This document provides a standardized method for calculating heat losses from domestic hot water generation systems. It defines inputs, outputs, and the calculation method. The calculation method covers domestic hot water requirements in all buildings and includes determining hot water demand, distribution losses, storage losses, and generation losses. Reference standards for components are provided. The symbols and units used in calculations are standardized.
This document is a list of 31 reports, analyses, evaluations, memos and commissioning reports prepared by Dan OLARU for Cernavoda Unit 1 Nuclear Power Plant. The documents cover topics such as thermalhydraulic analyses of systems, evaluations of equipment changes, commissioning tests performed, and decay heat calculations. They were produced between 1994 and 2002 to support the safe operation of Cernavoda Unit 1.
Thermal analysis of cpu with variable baseplate heat sink using cfdeSAT Publishing House
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology.
This document provides an overview of European directives and standards related to energy efficiency in buildings. It summarizes key directives such as the Energy Performance of Buildings Directive (EPBD) from 2002, which established requirements for calculating a building's energy performance and issuing energy performance certificates. It also discusses the directive on efficiency requirements for new hot water boilers from 1992. The document explains concepts such as a building's energy balance and performance index, and provides examples of best practices from different European countries.
Design of a low cost temperature controller for high temperature furnaces use...eSAT Publishing House
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology.
The document discusses several sustainable energy projects at NJIT, including upgrades to the campus-wide control system involving demand-based HVAC, lighting, and building controls. Specific buildings mentioned include the Campus Center, Fenster Hall, GITC, Oak Hall, and Weston Hall. Features described include variable speed pumping and cooling, chilled water reset, and heat recovery systems. Performance data and energy savings from the projects are presented.
An update on SAP, Code and Part L requirements and proposed updates. SAP assessments in detail, and SAP case studies for Part L compliance, Code for Sustainable Homes levels 4 and 5 (zero carbon).
This document discusses energy auditing of boilers. It describes the requirements of an efficient boiler and outlines two methods for evaluating boiler efficiency: the direct method which compares energy input and output, and the indirect method which accounts for losses. Key measurements are outlined for both methods. Factors affecting boiler performance are also summarized such as cleaning, water treatment, and fuel quality.
Potential Energy Savings from the Increased Application of Heating Controls i...Leonardo ENERGY
This document presents the methodology and results of an analysis assessing the potential energy savings from increased adoption of heating controls in residential buildings across the European Union. The analysis developed a spreadsheet tool to estimate energy savings from four different heating control packages being adopted in EU countries from now until 2030. The tool calculates potential savings at the country level and EU total based on data on current heating systems, controls, and the housing stock. The results show that enhanced adoption of heating controls could lead to annual energy savings of over 50TWh, fuel bill savings of €4.3 billion, and carbon dioxide reductions of nearly 12 million tonnes by 2030 at the EU level.
This document is a list of 31 reports, analyses, evaluations, memos and commissioning reports prepared by Dan OLARU for Cernavoda Unit 1 Nuclear Power Plant. The documents cover topics such as thermalhydraulic analyses of systems, evaluations of equipment changes, commissioning tests performed, and decay heat calculations. They were produced between 1994 and 2002 to support the safe operation of Cernavoda Unit 1.
Thermal analysis of cpu with variable baseplate heat sink using cfdeSAT Publishing House
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology.
This document provides an overview of European directives and standards related to energy efficiency in buildings. It summarizes key directives such as the Energy Performance of Buildings Directive (EPBD) from 2002, which established requirements for calculating a building's energy performance and issuing energy performance certificates. It also discusses the directive on efficiency requirements for new hot water boilers from 1992. The document explains concepts such as a building's energy balance and performance index, and provides examples of best practices from different European countries.
Design of a low cost temperature controller for high temperature furnaces use...eSAT Publishing House
IJRET : International Journal of Research in Engineering and Technology is an international peer reviewed, online journal published by eSAT Publishing House for the enhancement of research in various disciplines of Engineering and Technology. The aim and scope of the journal is to provide an academic medium and an important reference for the advancement and dissemination of research results that support high-level learning, teaching and research in the fields of Engineering and Technology. We bring together Scientists, Academician, Field Engineers, Scholars and Students of related fields of Engineering and Technology.
The document discusses several sustainable energy projects at NJIT, including upgrades to the campus-wide control system involving demand-based HVAC, lighting, and building controls. Specific buildings mentioned include the Campus Center, Fenster Hall, GITC, Oak Hall, and Weston Hall. Features described include variable speed pumping and cooling, chilled water reset, and heat recovery systems. Performance data and energy savings from the projects are presented.
An update on SAP, Code and Part L requirements and proposed updates. SAP assessments in detail, and SAP case studies for Part L compliance, Code for Sustainable Homes levels 4 and 5 (zero carbon).
This document discusses energy auditing of boilers. It describes the requirements of an efficient boiler and outlines two methods for evaluating boiler efficiency: the direct method which compares energy input and output, and the indirect method which accounts for losses. Key measurements are outlined for both methods. Factors affecting boiler performance are also summarized such as cleaning, water treatment, and fuel quality.
Potential Energy Savings from the Increased Application of Heating Controls i...Leonardo ENERGY
This document presents the methodology and results of an analysis assessing the potential energy savings from increased adoption of heating controls in residential buildings across the European Union. The analysis developed a spreadsheet tool to estimate energy savings from four different heating control packages being adopted in EU countries from now until 2030. The tool calculates potential savings at the country level and EU total based on data on current heating systems, controls, and the housing stock. The results show that enhanced adoption of heating controls could lead to annual energy savings of over 50TWh, fuel bill savings of €4.3 billion, and carbon dioxide reductions of nearly 12 million tonnes by 2030 at the EU level.
This document provides details on the design of an integrated sustainable building in Beijing, China. It discusses the environmental conditions, HVAC system selection, and other building aspects. A geothermal borefield was designed to support a water source variable refrigerant flow (WS VRF) system. The WS VRF system was chosen over a ground source heat pump system due to its higher performance, control capabilities, and lower noise levels. The design aims to meet ASHRAE standards while minimizing life cycle costs and environmental impacts.
Development of a Bench-Top Air-to-Water Heat Pump Experimental ApparatusCSCJournals
The document describes the development of a bench-top air-to-water heat pump experimental apparatus for educational purposes. Key features include:
- It demonstrates thermodynamics and heat transfer concepts through the vapor compression refrigeration cycle.
- It has instrumentation to display measurements and interface with a computer for data acquisition. Safety features like overcurrent protection are included.
- It was designed to heat 10°C of water using a condensing unit, evaporator, expansion valve, and other refrigeration components sized to meet power constraints.
- A control system with pressure transducers, microprocessor, and solid state relays monitors and operates the compressor and fans based on pressure levels.
- Performance
South Carolina Research Authority 2010 M2G CertificationCharles Rice
1) The document evaluates Greffen Systems' M2G boiler controller, which claims to reduce gas/oil consumption and costs by more accurately controlling boiler conditions. It does this by reducing unnecessary burner firings.
2) Field tests at various facilities found the controller reduced energy consumption by 10-17%, with average savings of 12-15%. Installation takes 2-4 hours.
3) Based on the evaluation, interviews, and industry standards compliance, the reviewer recommends approving the M2G controller for use in South Carolina facilities.
NC State is moving towards a more centralized distribution system for utilities including steam, chilled water, and electricity. There are currently 5 steam and chiller plants and 3 electrical substations that produce and distribute these utilities to buildings on campus. Centralized distribution systems are more energy efficient, environmentally friendly, reliable and cost effective than individual systems in each building. They work by producing steam, hot water or chilled water at a central plant then piping it underground to buildings for heating and cooling needs.
The document analyzes the heating requirements of a classic four-story brownstone building located in New York City. It details the building schematics and calculates the heat losses through the walls, windows, doors, and roof to determine the overall heating load. The analysis is conducted over an entire year, individual months, and a sample autumn day. It establishes parameters such as insulation levels and temperature requirements. Equations for heat transfer via conduction are used to calculate losses. The results will be used to design a heating system capable of maintaining a comfortable temperature year-round.
This document provides an overview of boiler energy audits. It discusses the importance of auditing boilers to evaluate performance and efficiency over time. The direct and indirect methods for evaluating boiler efficiency are described. Key factors that affect boiler operating efficiency are outlined, such as fuel quality, air supply, and boiler maintenance. Typical losses in boilers like dry flue gas and moisture are also summarized. Finally, the document lists some energy conservation opportunities for boilers like reducing excess air and stack temperatures.
The document describes REMKO's line of smart heat pumps. It discusses their intelligent and efficient air/water systems for heating and cooling. The WKF series is highlighted, including the WKF-compact model which has an integrated 300-liter domestic water tank. REMKO heat pumps use inverter technology to adapt output based on demand and can provide up to 75% of heating from air, making them independent of oil and gas. They are suitable for new and existing buildings.
This document presents the design of a liquid cooling system to retrofit data center server boards. It aims to provide a more efficient cooling solution than existing air cooling methods. The design uses microchannel heat sinks attached to heat-generating components, through which water is pumped in a series configuration. Testing was conducted to measure temperature reductions and compare actual thermal resistance to calculated values. While preliminary results show feasibility, additional testing is still needed to fully validate the design's effectiveness in removing necessary heat loads. The document provides background on data center cooling needs, advantages of liquid over air cooling, details of the microchannel heat sink design, and the thermal analysis conducted to optimize the design parameters.
This document provides an overview of power supply systems, including:
1) Electricity is generated at power stations and transmitted through high voltage transmission networks to load centers, where the voltage is stepped down for distribution through lower voltage networks to consumers.
2) Planning, construction, operation and maintenance of power supply systems require huge capital investments and operating costs to ensure a highly reliable electricity supply.
3) Generation, transmission, and distribution each represent significant portions of total system investment, with generation requiring the largest portion at around 50% of costs.
Bca j energy efficiency uq mech4460 lecture 2013Ken Thomson
The lecture was provided to 3-4 years students doing the Course Mech4460 - Energy & Environment at the University of Queensland. The aim was to introduce energy efficiency and energy efficiency regulations in the built Environment.
Combustion technology for generating energy from wasteTung Huynh
The document describes a new waste incineration plant, Line 4, built by I/S Reno Nord in Aalborg, Denmark. The plant was designed to process 20 metric tons of waste per hour into heat and electricity more efficiently than previous lines, while meeting strict emission regulations. It included a grate-fired furnace, steam boiler and turbine system, flue gas cleaning, and was built between 2004-2005 with performance testing completed in late 2005. The plant aims to efficiently convert the region's waste into thermal energy.
The presentation gives an idea about the primary requirements for the establishment of a coal based THERMAL POWER STATION. The estimates are quite fair.
This document summarizes a field study conducted in Minnesota to evaluate the energy savings and performance of an intelligent, networked water heater controller. Over 30 controllers were installed on electric and gas water heaters across the state. Detailed monitoring was conducted on 10 sites to analyze the impact on energy use profiles, hot water delivery, and savings. Preliminary results found energy savings of up to 15% from reduced standby losses, lower tank temperatures, and eliminating unnecessary reheats. Further monitoring through summer 2017 will assess annual savings with the goal of validating the technology for utility rebate programs.
The document describes the technical characteristics and assumptions that will be used to model new natural gas combined-cycle power plants in the Northwest Power Planning Council's fifth power plan. A typical plant would consist of one or more gas turbines paired with a heat recovery steam generator and steam turbine to produce between 270-540 megawatts. Combined-cycle plants have high efficiency and low emissions compared to other fossil fuel technologies. While combined-cycle plants are an important part of the region's power supply, issues like volatile natural gas prices, water consumption, and carbon dioxide production require ongoing assessment.
This document summarizes research on cold-climate air-source heat pumps conducted in Minnesota homes. Eight heat pumps were monitored, including six ducted whole-home systems and two ductless mini-split systems. The heat pumps performed well down to 5-10 degrees Fahrenheit for ducted systems and below -13F for ductless. Annual COPs were 1.2-2.1, providing energy savings of 40-60% compared to electric resistance or propane heating. Paybacks were estimated at 6 years or less when paired with replacing an existing heating or cooling system. Further research is needed to optimize controls and expand applications to multifamily buildings.
Energy modelling of a three-story primary school building located in Phoenix,...Kirtan Gohel
Energy modelling of a three-story primary school building in Phoenix, Arizona was conducted using HAP software to analyze the building's heating and cooling loads under different scenarios. In scenario 1 with a VAV rooftop system, significant cooling loads were found from May to September with no heating loads, indicating hot summer conditions. Scenario 2 compared VVT and VRF systems, finding the VRF system more efficient and economical. Scenario 3 modified the gym orientation and schedules, significantly reducing energy usage and annual costs.
Water cooled minichannel heat sinks for microprocessor cooling: Effect of fin...Danial Sohail
Heat sink with different fin spacing mounted on a microprocessor were tested for their heat removing capabilities by varying coolant flow rates over them
1/3/2016 Raising the temperature of the UK heat pump market: Learning lessons...Matthew Hannon
The document discusses lessons that can be learned from Finland's successful adoption of heat pumps to help the UK meet its climate targets. Finland now has over 500,000 heat pumps installed, providing 6% of its heat. There are similarities between current Finnish and targeted UK (2030) heat pump usage. Key factors driving Finland's growth include policies incentivizing efficiency upgrades and new construction, regulations requiring efficient buildings, and funding energy innovation. The document recommends the UK adopt similar policies around new builds, retrofits, long-term incentives, focusing on off-grid homes, and increasing investment in heat pump technology innovation.
Braden Haggerty Underwater Filmming and Dive/Water Safety ResumeBraden Haggerty
Braden Haggerty is a Vancouver based freelance professional underwater camera operator & photographer. This is Braden's Underwater Filmming and Dive/Water Safety resume.
Problem Gambling Forum: Meeting in the Middle
Presented by ABACUS Counselling Training & Supervision Ltd to the Problem Gambling National Provider Forum May 2012
This document provides details on the design of an integrated sustainable building in Beijing, China. It discusses the environmental conditions, HVAC system selection, and other building aspects. A geothermal borefield was designed to support a water source variable refrigerant flow (WS VRF) system. The WS VRF system was chosen over a ground source heat pump system due to its higher performance, control capabilities, and lower noise levels. The design aims to meet ASHRAE standards while minimizing life cycle costs and environmental impacts.
Development of a Bench-Top Air-to-Water Heat Pump Experimental ApparatusCSCJournals
The document describes the development of a bench-top air-to-water heat pump experimental apparatus for educational purposes. Key features include:
- It demonstrates thermodynamics and heat transfer concepts through the vapor compression refrigeration cycle.
- It has instrumentation to display measurements and interface with a computer for data acquisition. Safety features like overcurrent protection are included.
- It was designed to heat 10°C of water using a condensing unit, evaporator, expansion valve, and other refrigeration components sized to meet power constraints.
- A control system with pressure transducers, microprocessor, and solid state relays monitors and operates the compressor and fans based on pressure levels.
- Performance
South Carolina Research Authority 2010 M2G CertificationCharles Rice
1) The document evaluates Greffen Systems' M2G boiler controller, which claims to reduce gas/oil consumption and costs by more accurately controlling boiler conditions. It does this by reducing unnecessary burner firings.
2) Field tests at various facilities found the controller reduced energy consumption by 10-17%, with average savings of 12-15%. Installation takes 2-4 hours.
3) Based on the evaluation, interviews, and industry standards compliance, the reviewer recommends approving the M2G controller for use in South Carolina facilities.
NC State is moving towards a more centralized distribution system for utilities including steam, chilled water, and electricity. There are currently 5 steam and chiller plants and 3 electrical substations that produce and distribute these utilities to buildings on campus. Centralized distribution systems are more energy efficient, environmentally friendly, reliable and cost effective than individual systems in each building. They work by producing steam, hot water or chilled water at a central plant then piping it underground to buildings for heating and cooling needs.
The document analyzes the heating requirements of a classic four-story brownstone building located in New York City. It details the building schematics and calculates the heat losses through the walls, windows, doors, and roof to determine the overall heating load. The analysis is conducted over an entire year, individual months, and a sample autumn day. It establishes parameters such as insulation levels and temperature requirements. Equations for heat transfer via conduction are used to calculate losses. The results will be used to design a heating system capable of maintaining a comfortable temperature year-round.
This document provides an overview of boiler energy audits. It discusses the importance of auditing boilers to evaluate performance and efficiency over time. The direct and indirect methods for evaluating boiler efficiency are described. Key factors that affect boiler operating efficiency are outlined, such as fuel quality, air supply, and boiler maintenance. Typical losses in boilers like dry flue gas and moisture are also summarized. Finally, the document lists some energy conservation opportunities for boilers like reducing excess air and stack temperatures.
The document describes REMKO's line of smart heat pumps. It discusses their intelligent and efficient air/water systems for heating and cooling. The WKF series is highlighted, including the WKF-compact model which has an integrated 300-liter domestic water tank. REMKO heat pumps use inverter technology to adapt output based on demand and can provide up to 75% of heating from air, making them independent of oil and gas. They are suitable for new and existing buildings.
This document presents the design of a liquid cooling system to retrofit data center server boards. It aims to provide a more efficient cooling solution than existing air cooling methods. The design uses microchannel heat sinks attached to heat-generating components, through which water is pumped in a series configuration. Testing was conducted to measure temperature reductions and compare actual thermal resistance to calculated values. While preliminary results show feasibility, additional testing is still needed to fully validate the design's effectiveness in removing necessary heat loads. The document provides background on data center cooling needs, advantages of liquid over air cooling, details of the microchannel heat sink design, and the thermal analysis conducted to optimize the design parameters.
This document provides an overview of power supply systems, including:
1) Electricity is generated at power stations and transmitted through high voltage transmission networks to load centers, where the voltage is stepped down for distribution through lower voltage networks to consumers.
2) Planning, construction, operation and maintenance of power supply systems require huge capital investments and operating costs to ensure a highly reliable electricity supply.
3) Generation, transmission, and distribution each represent significant portions of total system investment, with generation requiring the largest portion at around 50% of costs.
Bca j energy efficiency uq mech4460 lecture 2013Ken Thomson
The lecture was provided to 3-4 years students doing the Course Mech4460 - Energy & Environment at the University of Queensland. The aim was to introduce energy efficiency and energy efficiency regulations in the built Environment.
Combustion technology for generating energy from wasteTung Huynh
The document describes a new waste incineration plant, Line 4, built by I/S Reno Nord in Aalborg, Denmark. The plant was designed to process 20 metric tons of waste per hour into heat and electricity more efficiently than previous lines, while meeting strict emission regulations. It included a grate-fired furnace, steam boiler and turbine system, flue gas cleaning, and was built between 2004-2005 with performance testing completed in late 2005. The plant aims to efficiently convert the region's waste into thermal energy.
The presentation gives an idea about the primary requirements for the establishment of a coal based THERMAL POWER STATION. The estimates are quite fair.
This document summarizes a field study conducted in Minnesota to evaluate the energy savings and performance of an intelligent, networked water heater controller. Over 30 controllers were installed on electric and gas water heaters across the state. Detailed monitoring was conducted on 10 sites to analyze the impact on energy use profiles, hot water delivery, and savings. Preliminary results found energy savings of up to 15% from reduced standby losses, lower tank temperatures, and eliminating unnecessary reheats. Further monitoring through summer 2017 will assess annual savings with the goal of validating the technology for utility rebate programs.
The document describes the technical characteristics and assumptions that will be used to model new natural gas combined-cycle power plants in the Northwest Power Planning Council's fifth power plan. A typical plant would consist of one or more gas turbines paired with a heat recovery steam generator and steam turbine to produce between 270-540 megawatts. Combined-cycle plants have high efficiency and low emissions compared to other fossil fuel technologies. While combined-cycle plants are an important part of the region's power supply, issues like volatile natural gas prices, water consumption, and carbon dioxide production require ongoing assessment.
This document summarizes research on cold-climate air-source heat pumps conducted in Minnesota homes. Eight heat pumps were monitored, including six ducted whole-home systems and two ductless mini-split systems. The heat pumps performed well down to 5-10 degrees Fahrenheit for ducted systems and below -13F for ductless. Annual COPs were 1.2-2.1, providing energy savings of 40-60% compared to electric resistance or propane heating. Paybacks were estimated at 6 years or less when paired with replacing an existing heating or cooling system. Further research is needed to optimize controls and expand applications to multifamily buildings.
Energy modelling of a three-story primary school building located in Phoenix,...Kirtan Gohel
Energy modelling of a three-story primary school building in Phoenix, Arizona was conducted using HAP software to analyze the building's heating and cooling loads under different scenarios. In scenario 1 with a VAV rooftop system, significant cooling loads were found from May to September with no heating loads, indicating hot summer conditions. Scenario 2 compared VVT and VRF systems, finding the VRF system more efficient and economical. Scenario 3 modified the gym orientation and schedules, significantly reducing energy usage and annual costs.
Water cooled minichannel heat sinks for microprocessor cooling: Effect of fin...Danial Sohail
Heat sink with different fin spacing mounted on a microprocessor were tested for their heat removing capabilities by varying coolant flow rates over them
1/3/2016 Raising the temperature of the UK heat pump market: Learning lessons...Matthew Hannon
The document discusses lessons that can be learned from Finland's successful adoption of heat pumps to help the UK meet its climate targets. Finland now has over 500,000 heat pumps installed, providing 6% of its heat. There are similarities between current Finnish and targeted UK (2030) heat pump usage. Key factors driving Finland's growth include policies incentivizing efficiency upgrades and new construction, regulations requiring efficient buildings, and funding energy innovation. The document recommends the UK adopt similar policies around new builds, retrofits, long-term incentives, focusing on off-grid homes, and increasing investment in heat pump technology innovation.
Braden Haggerty Underwater Filmming and Dive/Water Safety ResumeBraden Haggerty
Braden Haggerty is a Vancouver based freelance professional underwater camera operator & photographer. This is Braden's Underwater Filmming and Dive/Water Safety resume.
Problem Gambling Forum: Meeting in the Middle
Presented by ABACUS Counselling Training & Supervision Ltd to the Problem Gambling National Provider Forum May 2012
Problem Gambling Forum The Problem Gambling / Alcohol and other Drug Interfaceactsconz
Problem Gambling Forum The Problem Gambling / Alcohol and other Drug Interface
Presented by ABACUS Counselling Training & Supervision Ltd to the Problem Gambling National Provider Forum May 2012
This document contains messages from various individuals numbered #95 through #? discussing past experiences, relationships, and goals for defending an unspecified title as a team. The messages range from reflections on pre-sobriety days to challenges to raise pay and discussions of past romantic encounters.
Community workers play an important role in society by helping those in need and strengthening neighborhoods. They assist individuals and families facing challenges such as poverty, homelessness, substance abuse, and more. Through compassion and dedicated service, community workers improve lives and foster supportive communities.
Problem Gambling Treatment; the future arrives!actsconz
Problem Gambling Treatment; the future arrives!
Presented by Dr Sean Sullivan, ABACUS Counselling Training and Supervision Ltd at the 2012 Cutting Edge Conference, Wellington, New Zealand.
The impact of the revision of the EPBD on energy savings from the use of BACSLeonardo ENERGY
Specific requirements in the revised EPBD concerning building automation and control systems (BACS) will ensure that the European Union reduces building energy consumption significantly further and faster than if the Directive was implemented without BACS. In this webinar of the BACS Academy, Paul Waide, the author of the recent study “The impact of the revision of the EPBD on energy savings from the use of building automation and controls”, will provide the attendants with valuable information on how to effectively transform words into actions.
Welcome to International Journal of Engineering Research and Development (IJERD)IJERD Editor
journal publishing, how to publish research paper, Call For research paper, international journal, publishing a paper, IJERD, journal of science and technology, how to get a research paper published, publishing a paper, publishing of journal, publishing of research paper, reserach and review articles, IJERD Journal, How to publish your research paper, publish research paper, open access engineering journal, Engineering journal, Mathemetics journal, Physics journal, Chemistry journal, Computer Engineering, Computer Science journal, how to submit your paper, peer reviw journal, indexed journal, reserach and review articles, engineering journal, www.ijerd.com, research journals,
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This document presents a mathematical thermal model of a house to analyze temperature variation. It describes a simple rectangular house with one room and gable roof situated in a cold region. The model includes a thermostat and electric heater to control temperature. It analyzes heat transfer through walls and windows to calculate indoor temperature changes based on outdoor temperature. Results show indoor temperature varies according to climate and heating, while a system meter monitors electricity costs of operating the heater over time. The thermal model provides a way to study HVAC systems and improve house thermal design.
An approach to evaluate the heat exchanger retrofit for installed industrial ...eSAT Journals
Abstract This paper is the first part of a two-part study aiming to introduce a new integrated approach to evaluate the techno-economic value of recuperator retrofit on existing gas turbine engines. The original gas turbines are designed for combined cycles so that the pressure ratios are moderate to secure suitable exhaust temperatures. One way to enhance the thermal efficiency of some gas turbines is by using recuperation to recover some of the exhaust heat. In this part, the developed model is described and implemented for two gas turbine engines so the obtained characteristics are evaluated against the actual data. The new approach will assist users to select the suitable gas turbine models with favorable recuperator characteristics based on a technical and economic prospective. Besides, the performance results are used to design an appropriate shell and tube heat exchanger. Moreover, a new technique has been established to define the typical heat exchanger parameters in order to ensure the highest possible improvements over the original cycles. One of the main features of this method is that it depends only on the velocity of hot and cold heat exchanger streams from which the rest of the heat exchanger design and performance characteristics were derived. Key Words: integrated approach, techno-economic value, recuperation, shell and tube heat exchanger, velocity
IRJET-Detailed Energy Audit in a Captive Cogeneration PlantIRJET Journal
D.Rajani Kant , B.Sudheer Prem Kumar, N.Ravi Kumar, R.Virendra,J.Suresh Babu " Detailed Energy Audit in a Captive Cogeneration Plant ", International Research Journal of Engineering and Technology (IRJET), Volume2,issue-01 April 2015.e-ISSN:2395-0056, p-ISSN:2395-0072. www.irjet.net
Abstract
The rate of exploitation of the energy resources has been expanding over time and resulted in reduction of fossil fuel reserves. Efficiency of all resources is crucial both in environmental and economic sense. Using energy inefficiently creates waste in all the world’s economies. It has environmental impacts with regional, local and global implications.The key object is to adopt energy management in every field in order to reduce the wastage of energy sources and cost effectiveness without affecting productivity and growth.
Numerically and CFD studies on shell and tube heat exchangersIRJET Journal
1) The document discusses numerically and CFD studies on shell and tube heat exchangers with different baffle layouts.
2) Kern's theoretical approach and ASPEN simulation software were used to model and analyze a shell and tube heat exchanger.
3) Simulation results showed that a single segmental baffle exhibits the best heat transfer rate and mass cost on the shell side, while helical baffles result in less fouling and longer operating lifetime due to less flow-induced vibration.
Design and Development of Cascade Refrigeration SystemIRJET Journal
1) The document describes the design and development of a cascade refrigeration system using R22 in the low temperature circuit (LTC) and R134a in the high temperature circuit (HTC).
2) Cascade refrigeration systems use two independent refrigeration cycles coupled together to achieve very low temperatures, below what is possible with a single-stage vapor compression cycle.
3) Key parameters analyzed include the refrigeration effect, compressor work, coefficient of performance (COP), and how improving the effectiveness of the cascade heat exchanger can increase COP.
The development of solar energy gas coupling system (scada) in buildingseSAT Journals
Abstract The system mainly use wall-mounted gas boiler and give priority in use of solar energy in order to maximize the utilization of solar resources. The excess heat will be added to domestic water when the heat for floor radiant heating is enough. The PLC of Siemens is set as slave computer in the monitoring system and it is used to collect thermal parameters such as temperature, flow rate, etc. by temperature sensors, pressure sensors and flow rate sensors. WinCC is set as the host computer to monitor the operating conditions of the entire system. Real-time tracing, monitoring and alarming function can be achieved based on the SQL database, which has realized archive management of the date. The system has been debugged after the whole experiment platform is completed, and the running state of the system shows that this system has high reliability and good stability. Keywords: Solar Energy, Gas, PLC, WinCC, Database
IRJET- Thermoelectrical Generator for Waste heat Recovery- ReviewIRJET Journal
This document reviews thermoelectric generators for recovering waste heat. It discusses how thermoelectric generators can directly convert waste heat into electrical energy in an environmentally friendly way. The document summarizes the operating principles of thermoelectric generators, which use the temperature difference across semiconductors to generate electricity. It also analyzes different heat exchanger designs and their impact on thermal uniformity and pressure drop when recovering heat from engine exhaust. Recovering only 30% of wasted heat could significantly improve engine efficiency.
Temperature Control for a Cryogenic Freezer for Bovine Semen Samples for Assi...IRJET Journal
This document describes a temperature control system for a cryogenic freezer used to freeze bovine semen samples. The system uses a PID controller in a pole placement scheme to track an internationally accepted freezing temperature profile. This is intended to increase sperm survival rates from the current 50% achieved with traditional freezing methods. The control system is designed around inexpensive, discrete components to provide an affordable alternative for cryogenic control applications like freezing bovine semen. Simulation results indicate the controller can successfully track the freezing profile and may increase sperm survival if certain efficiency improvements are made to the cryogenic freezer prototype.
“Optimization of battery Cooling system for electric vehicle using Simulation”IRJET Journal
This document discusses optimizing the battery cooling system for electric vehicles through simulation. It begins by discussing how battery thermal management systems (BTMS) directly impact electric vehicle performance and describes a CFD model that improves temperature analysis accuracy within battery packs. Liquid cooling systems are found to have higher heat conductivity and capacity than air cooling systems, improving battery performance and maintaining a higher state of charge for longer periods. The document then discusses the methodology, which involves 3D modeling, CFD analysis, simulation, and comparing results graphs. It establishes requirements for the battery pack model and analyzes battery heat generation based on electric current draw and state of charge.
Air Water System Design using Revit Mep for a Residential Buildingijtsrd
This document describes an air-water system design for a residential building using Revit MEP software. Heating and cooling load calculations were performed for the building spaces using Revit MEP. The peak cooling and heating loads were calculated for each space. These values were used to calculate the tonnage of refrigeration needed for each space and for the total building. Duct design was also performed using Revit MEP based on the calculated air flow rates for each space. The results determined that an HVAC system with a capacity of approximately 21.32 tons of refrigeration would be suitable to condition the residential building.
Hydraulic Oil Cooling with Application of Heat PipeIRJET Journal
1. The document discusses using heat pipes to cool hydraulic oil in systems. Heat pipes transfer heat from hot oil to fins more efficiently than conventional cooling methods.
2. A prototype hydraulic oil cooler was developed that uses 4 parallel heat pipe modules to transfer heat from hot oil to spiral radial fins, aided by a radial blower. Experimental results showed increased heat transfer rates and effectiveness with higher oil flow rates.
3. Using heat pipes for hydraulic oil cooling provides benefits like lower maintenance costs, reduced system size, and energy savings compared to other cooling methods. The experiments demonstrated the heat pipe cooler's ability to prevent hydraulic system overheating through efficient heat removal.
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Wi 11 tc-approval_version_pr_en_15316-3-3_domestic_hot_water_-_generation
1. Document type: European Standard
Document subtype:
Document stage: Formal Vote
Document language: E
C:Mine dokumenterTC 228WG 4WI 00228034TC versionN562_prEN 15316-3-3_WI00228034_2006-
08.doc STD Version 2.2
Doc. CEN/TC 228 N562 CEN/TC 228
Date: 2006-08
CEN/TC 228 WI 034
CEN/TC 228
Secretariat: DS
Heating systems in buildings — Method for calculation of system energy
requirements and system efficiencies — Part 3-3: Domestic hot water
systems, generation
Einführendes Element — Haupt-Element — Teil 3.3: Ergänzendes Element
Systèmes de chauffage dans les bâtiments — Élément central — Partie 3.3 : Élément complémentaire
ICS:
Descriptors:
2. prEN 15316-3-3:2006 (E)
2
Contents Page
1 Scope ......................................................................................................................................................5
2 Normative references ............................................................................................................................5
3 Terms and definitions ...........................................................................................................................6
4 Symbols and Units.................................................................................................................................6
5 Energy requirements of the domestic hot water system ..................................................................7
6 Hot water storage vessel heat loss......................................................................................................9
7 Primary circulation pipes................................................................................................................... 10
8 Heat generation energy requirements.............................................................................................. 11
9 Recoverable heat losses, recovered heat losses and unrecoverable heat losses...................... 14
Annex A (informative) Calculation of heat loss from a gas or oil fired boiler.......................................... 15
Annex B (informative) Thermal loss from a gas fired hot water storage heater..................................... 18
Annex C (informative) Thermal loss from an electrically heated hot water storage heater (with
continuous power on) ........................................................................................................................ 20
Annex D (informative) Thermal loss from an electrically heated hot water storage vessel (with
timed power on) .................................................................................................................................. 21
3. prEN 15316-3-3:2006 (E)
3
Foreword
This document prEN 15316-3-3:2005) has been prepared by Technical Committee CEN/TC 228 “Heating
systems in buildings”, the secretariat of which is held by DS.
The subjects covered by CEN/TC 228 are the following:
- design of heating systems (water based, electrical etc.);
- installation of heating systems;
- commissioning of heating systems;
- instructions for operation, maintenance and use of heating systems;
- methods for calculation of the design heat loss and heat loads;
- methods for calculation of the energy performance of heating systems.
Heating systems also include the effect of attached systems such as hot water production systems.
All these standards are systems standards, i.e. they are based on requirements addressed to the system as a
whole and not dealing with requirements to the products within the system.
Where possible, reference is made to other European or International Standards, a.o. product standards.
However, use of products complying with relevant product standards is no guarantee of compliance with the
system requirements.
The requirements are mainly expressed as functional requirements, i.e. requirements dealing with the function
of the system and not specifying shape, material, dimensions or the like.
The guidelines describe ways to meet the requirements, but other ways to fulfil the functional requirements
might be used if fulfilment can be proved.
Heating systems differ among the member countries due to climate, traditions and national regulations. In
some cases requirements are given as classes so national or individual needs may be accommodated.
In cases where the standards contradict with national regulations, the latter should be followed.
4. prEN 15316-3-3:2006 (E)
4
Introduction
This document is one of three documents that together describe methods for calculation of system energy
requirements and system efficiencies related to domestic hot water systems. In particular this document
describes methods for calculating the input energy requirements and energy losses for the generation units.
The user shall refer to other European standards or to National documents for input data and detailed
calculation procedures not provided by this standard.
Only the calculation method is normative. All the values necessary to complete the calculations are to be
given in a National Annex.
5. prEN 15316-3-3:2006 (E)
5
1 Scope
This standard is part of the method for calculation of system energy requirements and system efficiencies.
The scope of this specific part is to standardise the methods for calculation of the heat losses from the
domestic hot water generation system and it defines the:
⎯ inputs;
⎯ outputs;
⎯ calculation method.
This standard covers the domestic hot water requirements in all buildings.
The general approach to calculate energy consumptions and losses of domestic hot water systems is as
follows:
⎯ calculation of domestic hot water requirements of a dwelling, a zone or a building ( WQ );
⎯ calculation of heat losses due to the distribution or circulation of domestic hot water supplied ( dWQ , );
⎯ calculation of heat losses in hot water storage units ( sWQ , ) and heat losses due to the production or
generation ( gWQ , ).
In order to be coherent with calculation methods for space heating systems, emission losses representing
taps and control should be taken into account.
2 Normative references
The following referenced documents are indispensable for the application of this document. For dated
references, only the edition cited applies. For undated references, the latest edition of the referenced
document (including any amendments) applies.
EN 89, Gas-fired storage water heaters for the production of domestic hot water
EN 297, Gas-fired central heating boilers - Type B11 and B11BS boilers, fitted with atmospheric burners of
nominal heat input not exceeding 70 kW
EN 304, Heating boilers - Test code for heating boilers for atomizing oil burners
EN 483, Gas-fired central heating boilers - Type C boilers of nominal heat input not exceeding 70 kW
EN 625, Gas-fired central heating boilers - Specific requirements for the domestic hot water operation of
combination boilers of nominal heat input not exceeding 70 kW
EN 656, Gas-fired central heating boilers - Type B boilers of nominal heat input exceeding 70 kW but not
exceeding 300 kW
EN 677, Gas-fired central heating boilers - Specific requirements for condensing boilers with a nominal heat
input not exceeding 70 kW
IEC prEN 50440, Efficiency of electrical storage water heaters
prEN wi 9 part 2.2.1, Heating systems in buildings - Method for calculation of system energy requirements and
system efficiencies – Part 2.2.1: Space heating generation systems, Combustion systems
prEN wi 9 part 2.2.2, Heating systems in buildings - Method for calculation of system energy requirements and
system efficiencies – Part 2.2.2: Space heating generation systems, Heat pump systems
6. prEN 15316-3-3:2006 (E)
6
prEN wi 9 part 2.2.3, Heating systems in buildings - Method for calculation of system energy requirements and
system efficiencies – Part 2.2.3: Space heating generation systems, Thermal solar systems
prEN wi 9 part 2.2.4, Heating systems in buildings - Method for calculation of system energy requirements and
system efficiencies – Part 2.2.4: Space heating generation systems, The performance and quality of CHP
electricity and heat (incl. on-site and micro-CHP)
prEN wi 9 part 2.2.5, Heating systems in buildings - Method for calculation of system energy requirements and
system efficiencies – Part 2.2.5: Space heating generation systems, The performance and quality of district
heating and large volume systems
prEN wi 9 part 2.2.6, Heating systems in buildings - Method for calculation of system energy requirements and
system efficiencies – Part 2.2.6: Space heating generation systems, The performance of other renewables
heat and electricity
prEN wi 9 part 2.2.7, Heating systems in buildings - Method for calculation of system energy requirements and
system efficiencies – Part 2.2.7: Space heating generation systems, Biomass combustion systems
3 Terms and definitions
THIS SECTION HAS STILL TO BE PROVIDED BY SEPARATE GROUP WORKING ON
COMMON DEFINITIONS.
4 Symbols and Units
THE SYMBOLS AND UNITS ARE BEING CO-ORDINATED BY A SEPARATE GROUP. THESE SYMBOLS
AND UNITS TO BE BROUGHT IN LINE WITH THE AGREED LIST WHEN IT IS AVAILABLE. SYMBOLS IN
THE EQUATIONS THROUGHOUT THE DOCUMENT TO BE BROUGHT IN LINE.
For the purposes of this standard, the following symbols and units (see Table 1) and indices (see Table2)
apply:
Table 1 : Symbols and units
Symbol Name of quantity Unit
A area m
2
C specific heat capacity J/(kg K)
e system performance coefficient (expenditure factor) -
d diameter mm
f conversion factor -
L length m
M mass kg
N number of operating times -
t time, period of time s
T thermodynamic temperature K
Q quantity of heat, energy J
φ thermal power W
P electrical power W
U heat loss coefficient W/mK
7. prEN 15316-3-3:2006 (E)
7
V volume m
3
W electrical auxiliary energy J
x,y constants -
z running time h/d
α part -
η efficiency -
θ celsius temperature °C
λ heat conductivity W/mK
Table 2 : Indices
amb ambiant hydr hydraulic p pipe
ave average h heating energy P primary
corr corrected int internal r recovered
col collectif in input to system s storage
d distribution ind independent sb stand-by
e external l loss t total
em emission nom nominal out output from system
g generation, losses nhs non heated space W domestic hot water
gs gains PM pipe material x indices
5 Energy requirements of the domestic hot water system
The heat generator for a domestic hot water system must provide the energy required for meeting the hot
water demand and the losses in the system. The energy requirement on the heat generator is therefore equal
to the sum of the user hot water demand, the losses in the user outlet (if taken into account), the total losses
in the distribution system (including circulation loops and individual draw off pipes), losses in the hot water
storage vessel (if present), losses in the primary circulating pipes (if hot water storage vessel present) and
losses from the heat generator itself.
WhgWppWsWdW QQQQQQ ++++= ∑
where
WQ domestic hot water requirement(kWh/day) (see pr EN 15316-3-1)
WdQ heat loss from distribution system (kWh/day) (see pr EN 15316-3-2)
WsQ heat loss from storage vessel (if present)(kWh/day)
WppQ heat loss from primary pipes (if present) (kWh/day)
WhgQ heat loss from heat generator (kWh/day)
8. prEN 15316-3-3:2006 (E)
8
If the heat generator or generators also provide space heating then the performance of the heat generator
must be calculated separately for operation during the summer period, when the space heating demand is
zero, and the winter period, when both space heating and domestic hot water is being provided.
5.1 Domestic hot water systems using a single heat generator
If a single heat generator is used then the total heat requirement has to be provided from that heat generator.
5.2 Domestic hot water systems using multiple heat generators
If several heat generators are used to provide the domestic hot water energy requirement, the contribution
from each heat generator is calculated on the basis of the nominal output of each individual heat generator. If
any or all of these heat generators have separate primary pipe circuits then the primary pipe loss and the
auxiliary energy should be calculated separately for each circuit.
5.2.1 Domestic hot water systems using different types of heat generator (heat generators in series)
If the domestic hot water is heated by several different types of heat generator, the contribution of each
individual heat generator shall be determined. Normally it is assumed, that the domestic hot water can be
heated by a maximum of three heat generators: pre-heating by e.g. solar panels, base heating, and
supplementary heating to meet the peak load. The sum of all the contributions is by definition 1.0.
If heat energy is supplied to the domestic hot water system from other appliance types (e.g. exhaust air heat
pump, see prEN15243, prEN15316-4-3) (see also prEN15316-1). The remaining heat demand that is covered
by the supplementary heat generator (e.g. a boiler), is given by:
outgrv,w,solw,outgw,outgw,
*
QQQQ −−= (1)
where
outgw,
*
Q is the remaining generator useful heat output (kWh)
totwQ is the total heat requirement of the domestic hot water system (kWh)
outgw,rv,Q is the generator heat output of the domestic ventilation equipment for the domestic hot
water system (see prEN 15243), (kWh)
solw,Q is the energy contribution of the solar system for domestic hot water preparation (kWh).
5.2.2 Domestic hot water systems using multiple heat generators of a similar type (heat generators
in parallel)
If several heat generators are used to meet the heat required for the domestic hot water, the proportional
contribution igTW ,,α of each unit is calculated from the ratio of the nominal output of that unit to the total output
of the installation available for heating the domestic hot water.
i
i
igTWi QQ ∑=
1
,, *α (2)
9. prEN 15316-3-3:2006 (E)
9
For heating of the domestic water a number of heat generators (e.g. solar, boiler, heat pump, or electrical
ancillary heating) can be available. The total heat requirement for all loads must correspond to the total heat
output of all heat generators:
∑∑ =
kj
QQ kd,in,joutg,w, (4)
where
joutgWQ ,, is the energy output of heat generator j (kWh)
kdinQ ,, is the energy input to the distribution system k (kWh).
If several heat generators are present the total heat demand of the distribution system Qin,d,t is distributed
amongst the available heat generators. The calculations are to be performed independently for each heat
generator j on the basis of Qw,outg,j .
If a number of heat generators are used they are to be calculated in the sequence of their use in energy
generation.
6 Hot water storage vessel heat loss
The domestic hot water may be supplied from a storage vessel. This vessel may be directly heated i.e. by gas
or electricity, or may be indirectly heated by means of a heat generator. This clause considers indirectly
heated storage vessels. Directly heated storage vessels are considered to be heat generators and are
covered by clauses 6.3 and 6.4.
Heat losses occur from hot water storage vessels. These heat losses have an impact on the overall efficiency
of the domestic hot water system and contribute to the overall energy requirements of the building.
6.1 Indirectly heated hot water storage vessel
The storage heat loss from an indirectly heated hot water storage vessel can be obtained from the stand-by
heat loss of the vessel. The total heat dissipated from the storage vessel over the period of a year is quantified
as a loss.
The storage heat loss is calculated from a stand-by heat loss value, which is corrected for temperature
difference as follows:
bs
bss
AmbsW
sW QQ −
−
∗
−
=
,
,
,
)(
θ
θθ
(kWh/day) (2)
where
sW ,θ average temperature of stored water (o
C)
Ambθ average ambient temperature (o
C)
bss −,θ average temperature difference applied in stand-by heat loss tests (o
C)
bsQ − stand-by heat loss (kWh/day)
10. prEN 15316-3-3:2006 (E)
10
The stand-by heat loss has to be measured in accordance with a European or National Standard, i.e. pr
EN12897, appropriate for the vessel size and type. The measured stand-by heat loss is based on the actual
temperatures during the period of operation. The standard to be used for the measurement shall be specified
in a National Annex.
If the stand-by heat loss from the storage vessel is not available, a value can be calculated on the basis of an
equation of the form;
z
sbs VyxQ ∗+=− (kWh/day) (3)
where
sV vessel volume (litres)
zandyx, constants
Values for the constanst zandyx, shall be given in a National Annex.
The storage heat loss from older storage vessels can be estimated in a similar way, where values for the
constants zandyx, also shall be given in a National Annex. Alternatively a National Annex may specify the
stand-by heat loss based on storage volume and insulation type and thickness.
If the hot water storage vessel is located within the heated area of the building, part of the heat loss from the
vessel may be recovered (see 8).
Connecting pipes to the storage water heater may increase the heat loss from the storage vessel particularly if
they are not insulated. These losses are caused by circulation set up in the connecting pipes between the hot
water in the storage vessel and cooler water in the pipes away from the vessel. If these losses are to be taken
into account the method will be given in a National Annex.
7 Primary circulation pipes
Where the domestic hot water is supplied from an indirectly heated storage vessel, the heat energy is supplied
from a separate heat generator. The hot water storage vessel may be located adjacent to or remote from the
heat generator. Heat losses occur from the primary circulation pipes between the heat generator and the hot
water storage vessel, and these losses can be calculated by two different methods, either a simple estimation
method or a detailed calculation method.
The storage vessel may be incorporated into the appliance and the primary circulation pipe heat loss may
then be included in the overall appliance efficiency measurements. For gas appliances, with storage
incorporated and intended to be installed in single family dwellings, measurements to EN13203-2 will include
the primary circulation pipe heat loss.
7.1 Heat losses by a simple estimation method
A simple method for estimating the heat losses from primary circulation pipes is to use a fixed representative
value. Appropriate values shall be given in a National Annex. If a National Annex is not available or does not
include this value, this method cannot be applied.
7.2 Heat losses by a detailed calculation method
Methods for calculating the heat loss from pipes are given in pr EN15316-3-2. These methods shall be
followed for calculating the heat loss from primary circulation pipes.
11. prEN 15316-3-3:2006 (E)
11
For calculation of the heat losses from the primary circulation pipes, the actual length of the pipes should be
used, if available. If the detailed pipe network plan is not available, representative values for the pipe lengths
can be used. These values are to be given in a National Annex.
7.3 Auxiliary energy
Electrical energy is required for the circulation pump to overcome the pressure drop within the primary
circulation system between the heat generator and the hot water storage vessel. If the circulation pump is
contained within the heat generator, the energy required is considered as part of the auxiliary energy for the
heat generator. The auxiliary energy measure in accordance with an appropriate appliance standard for the
heat generator should then be used.
If a separate circulation pump is applied, the auxiliary energy requirement should be determined separately.
The circulation pump may also be used in the space heating system. Care must be taken to avoid duplicating
the energy requirement.
A simplified estimation method or a detailed calculation method may be applied to determine the energy
required for the pumps in the primary circulation system between the heat generator and the storage vessel.
Methods for calculating the auxiliary energy for circulation loops are given in pr EN15316-3-2. These methods
shall be followed for calculating the auxiliary energy from primary circulation pipes. Either the simplified
method or the detailed calculation method may be used. Details and default values to be used will be given in
a National Annex.
The specific power consumption of the pump should be used, if available. If the detailed pipe network plan
and pump specifications are not available, a representative value for the power consumption can be used.
This value shall be given in a National Annex.
8 Heat generation energy requirements
The domestic hot water requirement is provided by a heat generator, e.g. a liquid oil or gas fired boiler, a
direct gas fired or electrical fired storage water heater or a renewable energy source such as solar heating.
Energy labelling legislation requires efficiency measurements to be obtained for hot water heat generators to
be applied in single-family dwellings. These requirements are intended to be independent of the fuel source
and heat generator type and are therefore treated separately in 8.1.
Where domestic hot water generation systems are installed in buildings providing multi family accommodation
or in commercial buildings, the efficiency of the hot water generation is based on the appliance performance
standards appropriate for that appliance technology.
8.1 Heat generation losses for systems in single-family dwellings
The domestic hot water generation efficiency for single-family dwellings will be required to meet energy
labelling legislation. Standards developed to show compliance with this directive will incorporate test
procedures against three common hot water tapping cycles. The results of these tests will give a hot water
generation efficiency based on each of these tapping cycles. If the appliance is not intended to provide the hot
water requirement corresponding to all the tapping cycles, this will be identified in the appliance specification
and results will not be available for the corresponding hot water tapping cycle test.
It is not necessary to have results from all three tapping cycles. The method is based on an efficiency value
corresponding to the average tapping cycle and either the higher tapping cycle or the lower tapping cycle,
depending on whether the hot water energy requirement is above or below the average.
The domestic hot water generation efficiency related to the actual hot water use, can be obtained by linear
interpolation as follows:
12. prEN 15316-3-3:2006 (E)
12
For hot water use below the average, i.e. 21 QQQ corr <<
)845.5(*)(*267.0 122, corrgW Q−−−= ηηηη (5)
For hot water use above the average, i.e. 32 QQQ corr <<
)845.5(*)(*172.0 232, −−+= corrgW Qηηηη (6)
where;
1η efficiency at low tapping cycle
2η efficiency at average tapping cycle
3η efficiency at high tapping cycle
CorrQ corrected annual energy requirement (kWh/day)
If 1QQCorr < , use 1QQCorr =
If 3QQCorr > , test results may be available for higher tapping cycles. In this case, interpolation between 2Q
and the higher tapping cycle can be applied.
CorrQ is obtained by adding up the domestic hot water energy requirement and the heat losses in the system.
demWCorr QQQQ ++= (kWh/day) (7)
8.2 Heat generation losses for systems in other buildings
8.2.1 Heat losses from oil and gas fired boilers
8.2.1.1 General
The heat losses from the boiler iTWQ , and the auxiliary energy for the boiler HEgTWW ,, is calculated on the
basis of the nominal heat output nQ& , the efficiency η100% at the nominal output as shown in EU Directive
92/42, the stand-by heat loss qB,70, and the electrical input PHE of the auxiliary units in the boiler. These values
have to be determined either by measurements, e.g. in accordance with EN 304, EN 297, EN 483, EN 656,
EN 625 (for combination boilers) or EN 677 (for condensing boilers), or – if measurements are not available –
by fixed default values. Default values shall be provided in a National Annex.
8.2.1.2 Calculation of heat losses from boilers
The total heat loss from a boiler is based on the nominal output efficiency %100,gη , the stand-by heat loss sbgQ , ,
and the nominal heat output gQ
•
. The calculation method is given in Annex A.
A National Annex may specify default values if specific test results are not available.
13. prEN 15316-3-3:2006 (E)
13
For older boilers, for which the efficiency and the stand-by heat loss values may not be known, values may be
given in a National Annex.
8.2.1.3 Auxiliary energy
Auxiliary energy is the energy, other than fuel, required for operation of the burner, operation of the primary
circulation pump and operation of any other equipment related to the heat generation subsystem operation
and being an integral part of that system. Auxiliary energy shall be measured according to the product
standard. If there is no product standard then default values may be used. These will be detailed in a National
Annex.
Auxiliary energy, normally in the form of electrical energy, may partially be recovered as heat for space
heating or as energy transmitted to the water of the primary circulation circuit.
8.2.2 Direct gas fired domestic storage water heater
The efficiency of a direct gas fired domestic storage water heater should be obtained from tests in accordance
with EN 89. If no efficiency values are available, minimum values may be provided in a National Annex. These
values should not be lower than the default values given in Annex B.
The energy required to maintain the hot water temperature is assumed to be equal to the heat loss to the
surroundings. This value should be obtained from the test method specified in EN 89 and may be quoted by
the manufacturer. If no value is available, a default value shall be used. The default value is calculated on the
basis of the maximum value specified in EN 89 for the maintenance energy requirement. This is assumed to
be 20% less than the maximum value allowed.
The calculation method is described in annex B.
For older systems, where the manufacturer’s data is not available and measurements cannot be made, the
values to be used shall be given in a National Annex.
8.2.3 Direct electrical heated domestic storage water heaters
Electrically heated storage water heaters may be heated continuously or heated for a defined period of the
day.
8.2.3.1 Electrical heated domestic storage water heaters with power continuously on
Where the storage water heater is heated continuously the energy required can be considered as the sum of
the thermal losses of the electrical heater and energy demand (energy delivered + energy losses of the
distribution system).
The efficiency of a direct electrical fired domestic storage water heater shall be obtained from tests in
accordance with pr EN 50440.
The energy required to maintain the hot water temperature is assumed to be equal to the heat loss to the
surroundings. This value shall be obtained from the test method specified in pr EN 50440 and may be quoted
by the manufacturer.
The calculation method is described in Annex C. If values of the parameters for determining the stand-by heat
loss are not available, default values shall be provided in a National Annex.
For older systems, where the manufacturer’s data is not available and measurements cannot be made, the
values to be used shall be given in a National Annex.
14. prEN 15316-3-3:2006 (E)
14
8.2.3.2 Electrical heated domestic storage water heaters with power on timed
These appliances provide domestic hot water from a stored quantity of hot water. As the hot water is supplied
to the user outlets the hot water in the storage vessel is depleted. These appliances use power during a timed
period, usually to coincide with a low tariff period, to recover the stored hot water temperature.
The total energy of the hot water taken from the store is equal to the energy of the hot water requirement and
the loss in the distribution system. In addition energy is needed to overcome the losses from the hot water
storage vessel.
Efficiency, for electrical storage water heater is directly related to standby losses, that are measured in steady
conditions (EN 60379) or obtained from dynamic tests representing daily tapping patterns (pr EN 50440). The
method to be used is partly dependant on building type and the application of the hot water system. The
standard to be used will be given in a National Annex.
The calculation method, to estimate daily thermal losses corresponding to average design tapping cycles, is
described in Annex D. If values of the parameters for determining the daily thermal losses are not available,
default values shall be provided in a National Annex.
For older systems, where the manufacturer’s data is not available and measurements cannot be made, the
values to be used shall be given in a National Annex.
8.2.4 Heat losses from alternative generators
For systems, where all or part of the domestic hot water energy requirement is provided by heat generators
which are not oil or gas fired units or electrically heated systems, the efficiency of the heat generator is
determined from the relevant standard for the space heating systems, corresponding to the type of heat
generation system.
9 Recoverable heat losses, recovered heat losses and unrecoverable heat losses
The calculated heat losses are not all necessarily lost. Part of the heat losses, termed recoverable heat losses,
may be recovered and contribute to the space heating. The extent of recoverable heat losses depends on the
location of the pipes and the storage vessel. Only part of the recoverable losses are actually useful, however,
as recoverable losses can only be considered during periods of the year where there is a significant space
heating demand. Under some circumstances, the recoverable heat losses may add to the cooling load
required in a building. The proportion of the total recoverable losses that can be recovered is determined in pr
EN15315-1, for which the total recoverable losses are provided as an input.
Some of the auxiliary energy may be recovered as heat in the domestic hot water system, e.g. electrical
energy supplied to the circulation pump ends up as thermal energy in the water. The recovered heat losses
from the circulation pump transmitted to the water is taken into account directly as a reduction of the heat
losses.
In many systems, the same heat generator supplies space heating and heating for the domestic hot water.
Care shall be taken to ensure, that only those recoverable heat losses – which are not already accounted for
in the analysis of the space heating system – are taken into account in the analysis of the domestic hot water
system.
15. prEN 15316-3-3:2006 (E)
15
Annex A
(informative)
Calculation of heat loss from a gas or oil fired boiler
A.1 Calculation of total boiler heat loss
The total heat loss from a boiler is calculated from the heat loss during operation and the stand-by heat loss
as follows:
sbgglWglW QQQ ,%100,,, += (kWh/day) (A1)
where;
glWQ , total heat loss from boiler (kWh/day)
%100,,glWQ heat loss from boiler during operation for a 24 hour period (kWh/day)
sbgQ , stand-by heat loss from boiler (kWh/day)
A.2 Calculation of heat loss during boiler operation
The heat loss during the boiler operation period is calculated by:
%100%100%100,, /)/( ηη
•
∗−= QHHQ isglW (kWh/day) (A2)
where;
%100,,glWQ heat loss of the boiler for a day (kWh/day)
•
Q nominal heat output of boiler (kWh/day)
%100η efficiency of boiler at nominal output
sH higher calorific value of the fuel (kWh/kg or kWh/m3
)
iH lower calorific value of the fuel (kWh/kg or kWh/m3
)
A.3 Calculation of stand-by heat loss
The stand-by heat loss, QB, during periods where the boiler is not providing heat to a storage vessel or directly
to the domestic hot water, is calculated by:
16. prEN 15316-3-3:2006 (E)
16
iswnmumgBsb HHtQqQ /*)24(*)/(*)2070(/)(* %100,%100,,70, −−−= ηθθ (A3)
where;
Qsb stand-by heat loss of the boiler (kWh/day)
Qn nominal heat output of boiler (kW)
qB,70 stand-by heat loss at a boiler temperature of 70 °C and room temperature of 20 °C
Өg,m average boiler temperature during a stand-by period (°C)
Өu,m average room temperature (°C)
ttw,100% period of provision of energy for domestic hot water at nominal heat output (h/day)
During periods where the boiler provides space heating, the present stand-by heat losses are assumed to be
zero. Any heat energy generated during these periods and not used in the provision of space heating is
considered as heat losses in the assesment of the space heating energy requirements.
A.3.1 Average boiler temperature during a stand-by period
The average boiler temperature during a stand-by period depends on a number of factors. These include the
boiler controls, type of storage vessel (if applied) and associated space heating operation. For simplification,
the average boiler temperature during a stand-by period, mg,θ , is assumed to be 50°C, except for flow water
heaters where it is assumed to be 40 °C.
A.3.2 Load factor of a boiler
The load factor of a boiler is calculated as folows:
( )
( )gTWn
gTWsTWdTWceTWtw
gTW
TW
tQ
QQQQ
t
t
,
,,,,
,
%100
⋅
⋅+++
==
&
α
ϕ (A4)
where;
ϕTW part load factor of the boiler
t100% running time of the boiler at nominal heat output (hrs/day)
tTW,g duration of provision of energy for domestic hot water (hrs/day)
Qtw domestic hot water heat requirement (kWh/day)
QTW,ce heat losses from the domestic hot-water user outlets (kWh/day)
QTW,d heat losses from the domestic hot-water distribution system (kWh/day)
QTW,s heat losses from the domestic hot-water storage system (kWh/day)
Qn nominal heat output of the boiler (kW)
αTW,g, heat generator’s proportional contribution
17. prEN 15316-3-3:2006 (E)
17
A.3.3 Auxiliary energy for a boiler
The area related auxiliary energy requirement for operation of the boiler is calculated on the basis of the
auxiliary output PHE of the boiler measured at 100% full load in accordance with Council Directive 92/42, i.e. at
a volume flow rate corresponding to nominal heat output and a temperature difference between flow
temperature and return temperature of 15K. If the boiler is permanently equipped with a pump operated for
heating the domestic hot water in an external and indirectly heated storage vessel, PHE is determined at an
external hydraulic pressure loss of 10 kPa. If the boiler is permanently equipped with a circulation pump and a
storage vessel or heat transfer agent (a combination boiler), determination of PHE has to be carried out on this
combination boiler.
HETWHEHEgTW PPtQ **%100,, ϕ== (kWh/day) (A5)
where;
QTW,g,HE area-related auxiliary energy requirement for the boiler (kWh/day)
t100% running time of the boiler at nominal heat output (hrs/day)
PHE electrical power consumption of the boiler (kW)
ϕTW load factor of the boiler
If values of the parameters for determining the auxiliary energy requirement are not available, default values
shall be provided in a National Annex.
A.3.4 Nominal output efficiency of a boiler
Nominal output efficiency of a boiler, η100%, is determined from the nominal heat output of the boiler, nQ& in
(kW) at a test temperature of 70°C, as follows:
Standard boiler: η 100% = (85,0 + 2,0 .
log ( nQ& ))/100 (A6)
Low-temperature boiler: η 100% = (88,5 + 1,5 .
log ( nQ& ))/100 (A7)
Condensing boiler: η 100% = (92,0 + 1,0 .
log ( nQ& ))/100 (A8)
Improved condensing boiler: η 100% = (94,0 + 1,0 .
log ( nQ& ))/100 (A9)
18. prEN 15316-3-3:2006 (E)
18
Annex B
(informative)
Thermal loss from a gas fired hot water storage heater
The following minimum efficiency values can be used as default values:
⎯ 84% for all appliances, except for condensing appliances;
⎯ 98% for condensing appliances.
The energy required to maintain the hot water temperature is assumed to be equal to the heat loss to the
surroundings. This value is obtained by the test method specified in EN 89 and may be quoted by the
manufacturer. If no value is specified by the manufacturer, a default value shall be used. The default value is
calculated on the basis of the maximum value specified in EN 89 for the maintenance energy requirement and
is assumed to be 20% lower than the maximum value allowed.
The maintenance energy consumption, cmQ − , is calculated by:
For appliances of any nominal capacity with a heating-up time of 45 min. or more and for appliances with
a nominal capacity up to 200 l with a heating-up time less than 45 min.:
)015.011(8.0
67.0
QVQ scm ∗+∗∗=− (W) (B1)
or cmQ − = 250 W if the value given by the equation is lower
For appliances with a nominal capacity exceeding 200 l with a heating-up time less than 45 min.:
)017.09(8.0
67.0
QVQ scm ∗+∗∗=− (W) (B2)
or cmQ − = 250 W if the value given by the equation is lower
where;
sV nominal capacity (litres)
Q nominal heat input (W)
It is assumed that the total heat dissipated from the storage water heater is quantified as a loss.
The heat loss is calculated from the maintenance energy consumption and is corrected for temperature
difference as follows:
cm
cms
AmbWs
Ws QQ −
−
∗∗
−
= 24
)(
,θ
θθ
(Wh/day) (B3)
where;
Wsθ average water temperature in the storage water heater (o
C)
19. prEN 15316-3-3:2006 (E)
19
Ambθ average ambient temperature (o
C)
cms −,θ average temperature difference used for determination of the maintenance energy consumption (o
C)
cmQ − maintenance energy consumption (W)
20. prEN 15316-3-3:2006 (E)
20
Annex C
(informative)
Thermal loss from an electrically heated hot water storage heater (with
continuous power on)
The energy required to maintain the hot water temperature is assumed to be equal to the stand-by heat loss of
the storage water heater. This value is obtained by the test method specified in pr EN 50440 and may be
quoted by the manufacturer.
The stand-by heat loss per day, WsQ , is corrected to a temperature difference of 45 K and is calculated by:
1000
)(**16.1
*
)(
24
*
45
1
56
inoutactambM
Ws
C
E
tt
Q
θθθθ −
+
−
−
= (C1)
Mθ average water temperature in the storage water heater (o
C)
ambθ average ambient temperature (o
C)
56 tt − duration of test period (h)
1E maintenance energy consumption during test period (kWh)
actC xxxxxxxxxxxxxxxxxxx
inθ water temperature at each thermostat cut-in (o
C)
outθ water temperature at each thermostat cut-off (o
C)
21. prEN 15316-3-3:2006 (E)
21
Annex D
(informative)
Thermal loss from an electrically heated hot water storage vessel (with
timed power on)
This calculation method is used to predict the energy consumption of a hot water storage vessel relevant to
daily tapping cycles.
The energy consumption of electrical water-heater is calculated when adding:
• the energy demand at the entry of the water-heater (hot water demand and distribution losses)
• the thermal losses.
The hot water is thermally stratified within the hot water storage vessel, due to the fact that the heating up
period and hot water period are separated. The thermal losses can be considered as a function of the surface
of the storage water-heater that is adjacent to the hot part of the stored water and which therefore could loose
thermal energy to the environment surrounding the water heater.
The basis of the calculation is to consider the average value of the surface of the water that corresponds to
the part of the vessel that remains hot during a daily cycle.
The method is based on simplified hot water draw off schedules dividing the daily hot water demand into three
periods of morning, noon and evening.
The energy Eab is calculated as follows:
Fig D.1 Indication of the change in surface relevant to heat loss estimations due to hot water draw offs
n
0
*
prWATER
S
S
QEE
⎟
⎟
⎠
⎞
⎜
⎜
⎝
⎛
⋅+= (D1)
S
S0
t0 t1 t2 t3 t4 t5 t6
Morning demand
Noon demand
Evening
demand
Heating up
22. prEN 15316-3-3:2006 (E)
22
with
D
h
n
4
D
2hDS
2
0 ⋅⋅⋅π⋅+⋅⋅π= (D2)
=iE Energy corresponding to morning, noon or evening demand according to the simplified tapping pattern
1000
)1565(V16,1
EESWH
−⋅⋅
= (D3)
( ) )tt(S
24
1
S i1ii
7i
0i
*
−⋅= +
=
=
∫ (D4)
with
4
1
2
D
E
E
hDS
ESWH
i
i ⋅⋅⎟⎟
⎠
⎞
⎜⎜
⎝
⎛
−⋅⋅⋅= ππ (D5)
P
QE
tt
prWATER
45
+
=− (D6)
and ( )4556 tt8tt −−=− (D7)
where:
D external diameter (m)
H external high of the appliance (m)
n =1, 25 heat transfer coefficient
ti time switch for water withdrawal or heating up (h)
Qpr standardized value for thermal losses (kWh/24h)
V Rated capacity ( l )
P Power of the energy supply
Cm quantity of hot water delivered ( l )
EWATER Energy delivered regarding the tapping pattern considered (2,1 kWh, 5,85 kWh or 11,65 kWh)
S0 surface taken in account for calculation when the water heater is in hot conditions (m²)
S* surface of the appliance equivalent of a medium value for a daily cycle (m²)
Xi coefficient representing the relative quantity of energy delivered versus the maximum energy stored
EESWH maximum value of energy that could be stored in the appliance (kWh)
Example:
External diameter D = 0, 52 (m)
External high of the appliance h = 1, 42 (m)
Heat transfer coefficient n = 1, 25
Time switch for water withdrawal or heating up ti = 0 (s)
Standardized value for thermal losses Qpr = 1, 71 (kWh/24h)
Rated capacity V = 200 ( l )
Quantity of hot water delivered Cm [ l ]
P = 2, 2 (kW)
E WATER: Energy delivered regarding to the tapping pattern considered (2, 1 kWh, 5, 85 kWh or 11, 65 kWh)
23. prEN 15316-3-3:2006 (E)
23
Other parameters needed:
• Surface taken into account for calculation when the water heater is in hot condition S0 = 3,77 (m²)
• Surface of the appliance equivalent to the medium value for the daily cycle concerned S* (m²)
• Coefficient representing the relative quantity of energy delivered versus the maximum energy stored
Xi
• Maximum value of energy that could be stored in the appliance EESWH = 10, 44 kWh
Calculated figures Result with tapping pattern I Result with tapping pattern II
t1- t0 0,50 h 0,25
t2- t1 5,25 h 5,75
t3- t2 7,25 h 7,75
t4- t3 3,00 h 2,75
t5- t4 1,74 h 3,44
t6- t5 6,26 h 4,56
S0 3,77 m² 3,77 m²
SX 2,50 m² 2,42 m²
E 3,13 kWh 6,84 kWh
η 0,69 0,86