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Brainstorm some ways to use the cooling water exiting the condenser of a large power plant.

Short Answer

Expert verified
The cooling water can be used for district heating, agricultural purposes, aquaculture, and in other industrial processes.

Step by step solution

01

- Understand the Context

Recognize that the cooling water exiting the condenser in a power plant is often still relatively warm. This water, if not reused, can cause thermal pollution when discharged back into natural water bodies.
02

- Identify Potential Uses

Creatively brainstorm potential applications for the warm water that minimize environmental impact and possibly offer additional benefits.
03

- Reuse for Heating

The warm water can be used in district heating systems. This involves channeling the warm water to provide heating for residential and commercial buildings within the vicinity of the power plant.
04

- Agricultural Uses

Consider using the warm water for agricultural purposes such as irrigation or heating greenhouses, enabling year-round farming and boosting crop yields.
05

- Aquaculture

Utilize the warm water in aquaculture facilities for breeding fish or other aquatic organisms. The controlled warm temperatures can promote faster growth rates.
06

- Industrial Uses

Supply the warm water to nearby industrial facilities that require hot water for their processes, reducing their energy consumption for heating.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Thermal Pollution Prevention
When power plants discharge warm cooling water into natural water bodies, it can lead to thermal pollution. This is a serious environmental concern because it can harm aquatic life. Warm water decreases oxygen levels, which can stress or kill fish and other organisms. By reusing the warm water instead, we can minimize this impact.
Thermal pollution prevention involves:
  • Recycling the warm water into other useful applications instead of discharging it.
  • Utilizing heat exchangers to reclaim some of the heat before releasing the water.
  • Engaging in practices that reduce the temperature of water before it is reintroduced to natural bodies.

This approach not only protects ecosystems but also provides opportunities to harness the water's residual heat for beneficial purposes.
District Heating Systems
District heating systems are an excellent application for reused cooling water. In these systems, warm water from the power plant can be piped into residential and commercial areas to provide heating.
Benefits of district heating systems include:
  • Reduced reliance on individual boilers or heaters for each building, leading to overall energy savings.
  • A more sustainable and efficient use of energy resources.
  • Potentially lower heating costs for residents and businesses.

Implementing district heating leverages the thermal energy in the power plant’s cooling water, transforming waste heat into a useful resource.
Industrial Process Heat Integration
Industrial processes often require significant amounts of heat. By integrating the power plant’s warm cooling water, industrial facilities can reduce their energy consumption.
This heat integration can be applied in:
  • Preheating raw materials or feedwater in manufacturing processes.
  • Maintaining high temperatures in chemical reactions.
  • Washing and cleaning processes that require warm water.

Utilizing this otherwise wasted heat improves the energy efficiency of industrial operations, contributing to lower operational costs and reduced environmental impact.
Aquaculture Water Heating
Aquaculture, or fish farming, thrives in controlled environments. Warm cooling water from power plants can be used to maintain optimal water temperatures, promoting healthier and faster-growing fish.
Advantages in aquaculture include:
  • Accelerated growth rates of fish and other aquaculture species.
  • Increased productivity and profitability for aquaculture facilities.
  • A sustainable use of residual heat without additional fuel consumption.

By reusing warm water in aquaculture, we can contribute to food security while efficiently managing thermal energy.
Agricultural Irrigation
Agriculture can benefit greatly from the reuse of warm cooling water, particularly in regions facing water scarcity. This water can be used for irrigation, helping to extend the growing season and improve crop yields.
Using warm water for agriculture has several benefits:
  • Promotes the growth of certain crops that thrive better in warmer conditions.
  • Reduces the need for additional water heating in greenhouses.
  • Enables year-round farming opportunities in colder climates.

By integrating the warm water into irrigation systems, we support sustainable farming practices while also improving efficiency.

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Most popular questions from this chapter

Based on thermal efficiency, approximately two-thirds of the energy input by heat transfer in the steam generator of a power plant is ultimately rejected to cooling water flowing through the condenser. Is the heat rejected an indicator of the inefficiency of the power plant?

Superheated steam at \(18 \mathrm{MPa}, 560^{\circ} \mathrm{C}\), enters the turbine of a vapor power plant. The pressure at the exit of the turbine is \(0.06\) bar, and liquid leaves the condenser at \(0.045\) bar, \(26^{\circ} \mathrm{C}\). The pressure is increased to \(18.2 \mathrm{MPa}\) across the pump. The turbine and pump have isentropic efficiencies of 82 and \(77 \%\), respectively. For the cycle, determine (a) the net work per unit mass of steam flow, in \(\mathrm{kJ} / \mathrm{kg}\). (b) the heat transfer to steam passing through the boiler, in kJ per \(\mathrm{kg}\) of steam flowing. (c) the thermal efficiency. (d) the heat transfer to cooling water passing through the condenser, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of steam condensed.

Steam enters the turbine of a vapor power plant at 100 bar, \(520^{\circ} \mathrm{C}\) and expands adiabatically, exiting at \(0.08\) bar with a quality of \(90 \%\). Condensate leaves the condenser as saturated liquid at \(0.08\) bar. Liquid exits the pump at 100 bar, \(43^{\circ} \mathrm{C}\). The specific exergy of the fuel entering the combustor unit of the steam generator is estimated to be \(14,700 \mathrm{~kJ} / \mathrm{kg}\). No exergy is carried in by the combustion air. The exergy of the stack gases leaving the steam generator is estimated to be \(150 \mathrm{~kJ}\) per \(\mathrm{kg}\) of fuel. The mass flow rate of the steam is \(3.92 \mathrm{~kg}\) per \(\mathrm{kg}\) of fuel. Cooling water enters the condenser at \(T_{0}=20^{\circ} \mathrm{C}, p_{0}=\) \(1 \mathrm{~atm}\) and exits at \(35^{\circ} \mathrm{C}, 1 \mathrm{~atm}\). Develop a full accounting of the exergy entering the plant with the fuel.

Superheated steam at \(8 \mathrm{MPa}\) and \(480^{\circ} \mathrm{C}\) leaves the steam generator of a vapor power plant. Heat transfer and frictional effects in the line connecting the steam generator and the turbine reduce the pressure and temperature at the turbine inlet to \(7.6 \mathrm{MPa}\) and \(440^{\circ} \mathrm{C}\), respectively. The pressure at the exit of the turbine is \(10 \mathrm{kPa}\), and the turbine operates adiabatically. Liquid leaves the condenser at \(8 \mathrm{kPa}, 36^{\circ} \mathrm{C}\). The pressure is increased to \(8.6 \mathrm{MPa}\) across the pump. The turbine and pump isentropic efficiencies are \(88 \%\). The mass flow rate of steam is \(79.53 \mathrm{~kg} / \mathrm{s}\). Determine (a) the net power output, in \(\mathrm{kW}\). (b) the thermal efficiency. (c) the rate of heat transfer from the line connecting the steam generator and the turbine, in \(\mathrm{kW}\). (d) the mass flow rate of condenser cooling water, in \(\mathrm{kg} / \mathrm{s}\), if the cooling water enters at \(15^{\circ} \mathrm{C}\) and exits at \(35^{\circ} \mathrm{C}\) with negligible pressure change.

Steam enters the first turbine stage of a vapor power cycle with reheat and regeneration at \(32 \mathrm{MPa}, 600^{\circ} \mathrm{C}\), and expands to \(8 \mathrm{MPa}\). A portion of the flow is diverted to a closed feedwater heater at \(8 \mathrm{MPa}\), and the remainder is reheated to \(560^{\circ} \mathrm{C}\) before entering the second turbine stage. Expansion through the second turbine stage occurs to \(1 \mathrm{MPa}\), where another portion of the flow is diverted to a second closed feedwater heater at \(1 \mathrm{MPa}\). The remainder of the flow expands through the third turbine stage to \(0.15 \mathrm{MPa}\), where a portion of the flow is diverted to an open feedwater heater operating at \(0.15 \mathrm{MPa}\), and the rest expands through the fourth turbine stage to the condenser pressure of \(6 \mathrm{kPa}\). Condensate leaves each closed feedwater heater as saturated liquid at the respective extraction pressure. The feedwater streams leave each closed feedwater heater at a temperature equal to the saturation temperature at the respective extraction pressure. The condensate streams from the closed heaters each pass through traps into the next lower-pressure feedwater heater. Saturated liquid exiting the open heater is pumped to the steam generator pressure. If each turbine stage has an isentropic efficiency of \(85 \%\) and the pumps operate isentropically (a) sketch the layout of the cycle and number the principal state points. (b) determine the thermal efficiency of the cycle. (c) calculate the mass flow rate into the first turbine stage, in \(\mathrm{kg} / \mathrm{h}\), for a net power output of \(500 \mathrm{MW}\).

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