The document discusses fire protection requirements for external floating roof liquid storage tanks, specifically protecting the rim seal area from fires. It proposes an alternative fire suppression system using compressed air foam (CAF) created with nitrogen, which provides superior fire suppression abilities compared to traditional low expansion foam systems. The CAF system delivers foam at a higher application rate than NFPA standards require but fills the rim seal space faster. Testing and FM approvals confirm the CAF system can effectively suppress hydrocarbon and polar solvent fires in the rim seal area. The system design was submitted to the Oil Industry Safety Directorate for review and potential approval.
The document discusses sprinkler system design criteria for flammable and combustible liquid storage. It outlines the history of criteria development in NFPA 30 based on full-scale fire tests involving various liquids, containers, and storage arrangements. Key points include:
- NFPA 30 criteria are now based on over 155 fire tests, providing more options for liquids, containers, and protection methods.
- Tests examine factors like material properties, container design, storage setup, and sprinkler parameters to understand liquid burning behaviors and develop pass/fail criteria.
- Criteria have limitations given variability in liquids and potential fire scenarios not yet tested. Additional testing is still warranted.
This document summarizes guidelines for coal processing facilities from the World Bank Group. It discusses potential environmental impacts including air emissions, wastewater, hazardous materials, wastes, and noise. It provides recommendations to prevent and control fugitive particulate matter and gaseous emissions from coal storage, transfer, and processing activities through measures like dust suppression, enclosed conveyors, and emissions capture and filtration. It also discusses preventing fugitive emissions of volatile organic compounds, carbon monoxide, and hydrogen through monitoring, maintenance, vapor balancing, and secondary emissions controls. Significant carbon dioxide emissions can also be produced during synfuel manufacturing processes.
This document discusses guidelines for conducting integrity evaluations and assessing remaining life for chemical recovery boilers. It outlines a three-phase process: 1) Preliminary evaluation to collect information and identify degradation mechanisms and critical parts. 2) Non-destructive testing using methods like ultrasonics, dye penetrant, and metallography to verify damage. 3) Complementary analysis of test data to confirm findings, perform stress analysis, and issue a final report on structural condition and remaining life. It also provides recommendations for new boilers to facilitate future evaluations through data and sample collection during construction. The overall goal is to safely extend operating life through careful engineering assessments.
ABI Technology Systems provides integrated security systems including fire detection and suppression, access control, CCTV, and intrusion systems. They have a mission to design, supply, and install cost-effective, innovative technology systems through partnerships with suppliers and clients. They offer compressed air foam fire suppression systems which provide advantages over water such as faster fire knockdown, reduced risk to firefighters, and decreased property damage. ABI also provides system design, installation, monitoring, and maintenance for compressed air foam systems.
Guidelines for Engineering Design for Process Safety (Process Safety Guidelin...gurkanarifyalcinkaya
This document discusses pressure relief systems and emergency relief device design. It describes various scenarios that can lead to overpressure such as fires, blocked outlets, operational failures of equipment or utilities, and process upsets. These scenarios include fires, blocked flow, cooling water or power failure, and equipment malfunctions. The document emphasizes that relief systems should be designed to safely handle any scenarios that could cause overpressure while minimizing the need for relief devices to actuate. Regulations and industry standards provide guidelines for relief system design.
The document discusses sprinkler system design criteria for flammable and combustible liquid storage. It outlines the history of criteria development in NFPA 30 based on full-scale fire tests involving various liquids, containers, and storage arrangements. Key points include:
- NFPA 30 criteria are now based on over 155 fire tests, providing more options for liquids, containers, and protection methods.
- Tests examine factors like material properties, container design, storage setup, and sprinkler parameters to understand liquid burning behaviors and develop pass/fail criteria.
- Criteria have limitations given variability in liquids and potential fire scenarios not yet tested. Additional testing is still warranted.
This document summarizes guidelines for coal processing facilities from the World Bank Group. It discusses potential environmental impacts including air emissions, wastewater, hazardous materials, wastes, and noise. It provides recommendations to prevent and control fugitive particulate matter and gaseous emissions from coal storage, transfer, and processing activities through measures like dust suppression, enclosed conveyors, and emissions capture and filtration. It also discusses preventing fugitive emissions of volatile organic compounds, carbon monoxide, and hydrogen through monitoring, maintenance, vapor balancing, and secondary emissions controls. Significant carbon dioxide emissions can also be produced during synfuel manufacturing processes.
This document discusses guidelines for conducting integrity evaluations and assessing remaining life for chemical recovery boilers. It outlines a three-phase process: 1) Preliminary evaluation to collect information and identify degradation mechanisms and critical parts. 2) Non-destructive testing using methods like ultrasonics, dye penetrant, and metallography to verify damage. 3) Complementary analysis of test data to confirm findings, perform stress analysis, and issue a final report on structural condition and remaining life. It also provides recommendations for new boilers to facilitate future evaluations through data and sample collection during construction. The overall goal is to safely extend operating life through careful engineering assessments.
ABI Technology Systems provides integrated security systems including fire detection and suppression, access control, CCTV, and intrusion systems. They have a mission to design, supply, and install cost-effective, innovative technology systems through partnerships with suppliers and clients. They offer compressed air foam fire suppression systems which provide advantages over water such as faster fire knockdown, reduced risk to firefighters, and decreased property damage. ABI also provides system design, installation, monitoring, and maintenance for compressed air foam systems.
Guidelines for Engineering Design for Process Safety (Process Safety Guidelin...gurkanarifyalcinkaya
This document discusses pressure relief systems and emergency relief device design. It describes various scenarios that can lead to overpressure such as fires, blocked outlets, operational failures of equipment or utilities, and process upsets. These scenarios include fires, blocked flow, cooling water or power failure, and equipment malfunctions. The document emphasizes that relief systems should be designed to safely handle any scenarios that could cause overpressure while minimizing the need for relief devices to actuate. Regulations and industry standards provide guidelines for relief system design.
504314483-Fuel-Tank-Safety-Level-I-Presentation.pdfmram r
The document discusses efforts by the FAA and EASA to harmonize their fuel tank safety programs. It provides:
1) An overview of lessons learned from SFAR 88 reviews which revealed unexpected ignition sources and the difficulty of eliminating all risks, leading both agencies to adopt a balanced approach of continued ignition prevention efforts alongside reducing tank flammability.
2) Details on the status of ignition prevention reviews and corrective actions being implemented, as well as progress harmonizing flammability reduction standards and a plan to work towards agreement on retrofit requirements.
3) A summary that the combined ignition prevention and flammability reduction strategies should virtually eliminate the risk of future fuel tank explosions, and that FAA and E
This document provides information on thermal barriers and ignition barriers for the spray polyurethane foam industry. It defines what thermal barriers and ignition barriers are, where they are required by building codes, and options for selecting them. Thermal barriers are meant to prevent involvement of foam in a fire by limiting temperature rise, while ignition barriers provide some protection but are only allowed in attics and crawlspaces. Prescriptive options and tested alternative assemblies that meet code requirements are outlined. The document aims to help specifiers choose compliant foam and barrier systems.
The document discusses a proposal to issue commercial demonstration permits for certain emerging emission control technologies. It would allow up to 1,000 MW of pressurized fluidized bed units and units using multi-pollutant control technologies to be subject to less stringent emission standards in order to demonstrate the technologies. Similar standards from 2006 would be kept for SO2 and NOx to avoid weakening existing rules while providing flexibility. The document also discusses allowing advanced combustion controls for reducing NOx emissions to a standard of 1.0 lb/MWh.
This document discusses safety in the petroleum industry. It describes how petroleum products are classified based on their flash points and defines hazardous and non-hazardous areas. It also discusses processes for identifying hazards like HAZOP and HAZAN. The majority of the document focuses on fire protection facilities and systems for petroleum installations, including requirements for fire water systems, pumps, storage, hydrants and monitors. It provides design criteria and guidelines for fire protection facilities to minimize risk in the petroleum industry.
This document provides guidelines for oil and chemical plant layout and spacing to prevent property losses from fires and explosions. It recommends:
- Adequate spacing between units housing explosion/fire hazards to limit damage. Spacing should be based on hazard analysis and overpressure calculations.
- An open layout with blocks of 300x600 feet or less and access roads between for firefighting. Hazardous units should be separated or buffered.
- Increased spacing for very hazardous equipment like reactors, unless blast walls are used.
- Locating utilities, control rooms, services away from hazards.
Hazardous area classification and control of ignition sourceseldhoev
This document discusses hazardous area classification and control of ignition sources. It defines hazardous areas as any place where an explosive atmosphere may occur, and outlines the process to classify these areas into zones based on the likelihood and duration of an explosive atmosphere. The document provides guidance on identifying potential ignition sources and selecting appropriate equipment for use in the classified zones to ensure safety. It emphasizes the need to control ignition sources through design measures, work procedures, and proper equipment selection according to the zone classification.
This document provides information on PROTEGO deflagration flame arresters. It discusses their function of extinguishing flames in pipelines to protect equipment from deflagrations. It describes the modular design of the flame arrester unit and selection of the appropriate type and size based on the process parameters and explosion group of gases. Guidelines are provided on sizing, installation, selection, applications, and special designs available for critical services.
This document discusses the design of firefighting systems on board vessels. It begins by introducing common fires that occur at sea and the factors that cause fires. It then outlines the objectives and classification of fires. The document discusses functional requirements, extinguishing methods, fixed firefighting devices, and the central fire control station. It also covers engineering analysis, the location and availability of fire control plans, and the protection of special category spaces.
The document discusses how advanced oil and gas production processes like SAGD and fracking have increased requirements for lining systems that protect infrastructure from high heat, chemicals, and abrasion. Traditional lining materials are insufficient for these conditions and often fail. A new high-performance lining called Enviroline 405HTR was developed to address these issues with properties like chemical resistance up to 300°F, abrasion resistance, fast cure times, and low VOCs. It has been extensively tested and shown effective in real-world applications. Proper surface preparation and technical support are also important to maximize lining performance for oil and gas facilities.
The solution will provide a total volume of 225,000 liters of ME foam monitor, which will be released at a rate of up to 9,000 liters medium expansion foam per second, with a range of up to 100 meters. The system goes into full operation within five seconds after your drive. The figure below shows, graphically, a possible proposal for location and each set coverage radius. For this purpose, three sets of equipment would be used, providing 625,000 liters of medium expansion foam.
The document provides guidance on the internal cleaning of fuel tanks according to the following:
Section 1 defines applicable standards and regulations, as well as key terms. Section 2 outlines important safety requirements for cleaning processes. Section 3 details pre-cleaning inspection and isolation activities. Tanks must be emptied, connected pipes flushed, and isolation achieved before gas-freeing. Acceptable gas-freeing methods include filling the tank partially with water or using air/inert gas to purge vapors.
This document discusses methods for selecting the appropriate safety integrity level (SIL) for burner management systems. It presents a 7-step quantitative method to estimate consequences and likelihood of failures in order to determine the required SIL. The method involves calculating potential effect zones from vapor cloud explosions or pool fires, estimating personnel density within effect zones, performing layer of protection analyses to determine failure frequencies, and using these factors to calculate the probability of failure on demand and corresponding risk reduction factor to select the SIL. The document provides an example calculation for a natural gas-fired boiler to demonstrate how easily the 7-step method can be applied in practice.
This document discusses methods for selecting the appropriate safety integrity level (SIL) for burner management systems. It presents a 7-step quantitative method to estimate consequences and likelihood of failures in order to determine the required SIL. The method involves calculating potential effect zones from vapor cloud explosions or pool fires, estimating personnel density within effect zones, performing layer of protection analyses to determine failure frequencies, and using these factors to calculate the probability of failure on demand and corresponding risk reduction factor to select the SIL. The document provides an example calculation for a natural gas-fired boiler to demonstrate how easily the 7-step method can be applied in practice.
1) As a result of a catastrophic explosion at a fertilizer plant in West, Texas in 2013, OSHA is considering revisions to its Process Safety Management standard.
2) Two key areas OSHA may clarify are exemptions for flammable liquids in atmospheric storage tanks and using New Jersey's Toxic Catastrophe Prevention Act as a model, which defines "catastrophic release" more broadly.
3) The revisions could affect aboveground tank owners by expanding coverage, requiring stricter staffing levels, and defining equipment deficiency timelines.
This document discusses lessons learned from recent deepwater riser projects and how risers can become more standardized industrial products. It describes an industrialization process for risers involving a technical hierarchy to systematically organize components. This allows for detailed failure mode and effects analysis (FMECA) and structured engineering. An example FMECA is provided for a hybrid riser tower (HRT) system. The analysis identified 2 high risks related to connections at the top and bottom of the HRT, in line with reliability data. Overall the FMECA found 194 medium risks and 437 low risks. The document advocates standardizing key riser design aspects like materials to improve cost effectiveness while meeting functional requirements.
5 Ways New Explosion Venting Requirements For Dust Collectors Affect YouCamfil APC
This article sums up what you need to know about the new NFPA 68 standard on explosion venting for combustible dusts. The information here can help you better understand what's changed in this revised standard and how it will affect your dust collection choices today and in the future.
This document discusses KLM Technology Group, which provides training and consulting services related to process plant equipment and operations. It focuses on training courses for process flares, including an introduction to process flares, advanced flare design/operation/troubleshooting courses, and a syllabus for an advanced flare systems course. The document provides information on flare types (elevated and ground), system components, design factors and considerations, and safety, environmental, and social requirements related to flare system design.
The document provides an overview of the MODU code, which recommends safety standards for mobile offshore drilling units. It discusses the reasons for specific MODU code requirements, including that MODUs are specialized vessels operating in dangerous conditions. The purpose of the MODU code is to minimize risks to the unit, personnel, and environment. The document outlines some proposed updates and amendments to the 2009 MODU code being considered in light of the Deepwater Horizon disaster, including strengthening construction requirements against fires and explosions, clarifying emergency responsibilities, and increasing liferaft standards.
504314483-Fuel-Tank-Safety-Level-I-Presentation.pdfmram r
The document discusses efforts by the FAA and EASA to harmonize their fuel tank safety programs. It provides:
1) An overview of lessons learned from SFAR 88 reviews which revealed unexpected ignition sources and the difficulty of eliminating all risks, leading both agencies to adopt a balanced approach of continued ignition prevention efforts alongside reducing tank flammability.
2) Details on the status of ignition prevention reviews and corrective actions being implemented, as well as progress harmonizing flammability reduction standards and a plan to work towards agreement on retrofit requirements.
3) A summary that the combined ignition prevention and flammability reduction strategies should virtually eliminate the risk of future fuel tank explosions, and that FAA and E
This document provides information on thermal barriers and ignition barriers for the spray polyurethane foam industry. It defines what thermal barriers and ignition barriers are, where they are required by building codes, and options for selecting them. Thermal barriers are meant to prevent involvement of foam in a fire by limiting temperature rise, while ignition barriers provide some protection but are only allowed in attics and crawlspaces. Prescriptive options and tested alternative assemblies that meet code requirements are outlined. The document aims to help specifiers choose compliant foam and barrier systems.
The document discusses a proposal to issue commercial demonstration permits for certain emerging emission control technologies. It would allow up to 1,000 MW of pressurized fluidized bed units and units using multi-pollutant control technologies to be subject to less stringent emission standards in order to demonstrate the technologies. Similar standards from 2006 would be kept for SO2 and NOx to avoid weakening existing rules while providing flexibility. The document also discusses allowing advanced combustion controls for reducing NOx emissions to a standard of 1.0 lb/MWh.
This document discusses safety in the petroleum industry. It describes how petroleum products are classified based on their flash points and defines hazardous and non-hazardous areas. It also discusses processes for identifying hazards like HAZOP and HAZAN. The majority of the document focuses on fire protection facilities and systems for petroleum installations, including requirements for fire water systems, pumps, storage, hydrants and monitors. It provides design criteria and guidelines for fire protection facilities to minimize risk in the petroleum industry.
This document provides guidelines for oil and chemical plant layout and spacing to prevent property losses from fires and explosions. It recommends:
- Adequate spacing between units housing explosion/fire hazards to limit damage. Spacing should be based on hazard analysis and overpressure calculations.
- An open layout with blocks of 300x600 feet or less and access roads between for firefighting. Hazardous units should be separated or buffered.
- Increased spacing for very hazardous equipment like reactors, unless blast walls are used.
- Locating utilities, control rooms, services away from hazards.
Hazardous area classification and control of ignition sourceseldhoev
This document discusses hazardous area classification and control of ignition sources. It defines hazardous areas as any place where an explosive atmosphere may occur, and outlines the process to classify these areas into zones based on the likelihood and duration of an explosive atmosphere. The document provides guidance on identifying potential ignition sources and selecting appropriate equipment for use in the classified zones to ensure safety. It emphasizes the need to control ignition sources through design measures, work procedures, and proper equipment selection according to the zone classification.
This document provides information on PROTEGO deflagration flame arresters. It discusses their function of extinguishing flames in pipelines to protect equipment from deflagrations. It describes the modular design of the flame arrester unit and selection of the appropriate type and size based on the process parameters and explosion group of gases. Guidelines are provided on sizing, installation, selection, applications, and special designs available for critical services.
This document discusses the design of firefighting systems on board vessels. It begins by introducing common fires that occur at sea and the factors that cause fires. It then outlines the objectives and classification of fires. The document discusses functional requirements, extinguishing methods, fixed firefighting devices, and the central fire control station. It also covers engineering analysis, the location and availability of fire control plans, and the protection of special category spaces.
The document discusses how advanced oil and gas production processes like SAGD and fracking have increased requirements for lining systems that protect infrastructure from high heat, chemicals, and abrasion. Traditional lining materials are insufficient for these conditions and often fail. A new high-performance lining called Enviroline 405HTR was developed to address these issues with properties like chemical resistance up to 300°F, abrasion resistance, fast cure times, and low VOCs. It has been extensively tested and shown effective in real-world applications. Proper surface preparation and technical support are also important to maximize lining performance for oil and gas facilities.
The solution will provide a total volume of 225,000 liters of ME foam monitor, which will be released at a rate of up to 9,000 liters medium expansion foam per second, with a range of up to 100 meters. The system goes into full operation within five seconds after your drive. The figure below shows, graphically, a possible proposal for location and each set coverage radius. For this purpose, three sets of equipment would be used, providing 625,000 liters of medium expansion foam.
The document provides guidance on the internal cleaning of fuel tanks according to the following:
Section 1 defines applicable standards and regulations, as well as key terms. Section 2 outlines important safety requirements for cleaning processes. Section 3 details pre-cleaning inspection and isolation activities. Tanks must be emptied, connected pipes flushed, and isolation achieved before gas-freeing. Acceptable gas-freeing methods include filling the tank partially with water or using air/inert gas to purge vapors.
This document discusses methods for selecting the appropriate safety integrity level (SIL) for burner management systems. It presents a 7-step quantitative method to estimate consequences and likelihood of failures in order to determine the required SIL. The method involves calculating potential effect zones from vapor cloud explosions or pool fires, estimating personnel density within effect zones, performing layer of protection analyses to determine failure frequencies, and using these factors to calculate the probability of failure on demand and corresponding risk reduction factor to select the SIL. The document provides an example calculation for a natural gas-fired boiler to demonstrate how easily the 7-step method can be applied in practice.
This document discusses methods for selecting the appropriate safety integrity level (SIL) for burner management systems. It presents a 7-step quantitative method to estimate consequences and likelihood of failures in order to determine the required SIL. The method involves calculating potential effect zones from vapor cloud explosions or pool fires, estimating personnel density within effect zones, performing layer of protection analyses to determine failure frequencies, and using these factors to calculate the probability of failure on demand and corresponding risk reduction factor to select the SIL. The document provides an example calculation for a natural gas-fired boiler to demonstrate how easily the 7-step method can be applied in practice.
1) As a result of a catastrophic explosion at a fertilizer plant in West, Texas in 2013, OSHA is considering revisions to its Process Safety Management standard.
2) Two key areas OSHA may clarify are exemptions for flammable liquids in atmospheric storage tanks and using New Jersey's Toxic Catastrophe Prevention Act as a model, which defines "catastrophic release" more broadly.
3) The revisions could affect aboveground tank owners by expanding coverage, requiring stricter staffing levels, and defining equipment deficiency timelines.
This document discusses lessons learned from recent deepwater riser projects and how risers can become more standardized industrial products. It describes an industrialization process for risers involving a technical hierarchy to systematically organize components. This allows for detailed failure mode and effects analysis (FMECA) and structured engineering. An example FMECA is provided for a hybrid riser tower (HRT) system. The analysis identified 2 high risks related to connections at the top and bottom of the HRT, in line with reliability data. Overall the FMECA found 194 medium risks and 437 low risks. The document advocates standardizing key riser design aspects like materials to improve cost effectiveness while meeting functional requirements.
5 Ways New Explosion Venting Requirements For Dust Collectors Affect YouCamfil APC
This article sums up what you need to know about the new NFPA 68 standard on explosion venting for combustible dusts. The information here can help you better understand what's changed in this revised standard and how it will affect your dust collection choices today and in the future.
This document discusses KLM Technology Group, which provides training and consulting services related to process plant equipment and operations. It focuses on training courses for process flares, including an introduction to process flares, advanced flare design/operation/troubleshooting courses, and a syllabus for an advanced flare systems course. The document provides information on flare types (elevated and ground), system components, design factors and considerations, and safety, environmental, and social requirements related to flare system design.
The document provides an overview of the MODU code, which recommends safety standards for mobile offshore drilling units. It discusses the reasons for specific MODU code requirements, including that MODUs are specialized vessels operating in dangerous conditions. The purpose of the MODU code is to minimize risks to the unit, personnel, and environment. The document outlines some proposed updates and amendments to the 2009 MODU code being considered in light of the Deepwater Horizon disaster, including strengthening construction requirements against fires and explosions, clarifying emergency responsibilities, and increasing liferaft standards.
KuberTENes Birthday Bash Guadalajara - K8sGPT first impressionsVictor Morales
K8sGPT is a tool that analyzes and diagnoses Kubernetes clusters. This presentation was used to share the requirements and dependencies to deploy K8sGPT in a local environment.
CHINA’S GEO-ECONOMIC OUTREACH IN CENTRAL ASIAN COUNTRIES AND FUTURE PROSPECTjpsjournal1
The rivalry between prominent international actors for dominance over Central Asia's hydrocarbon
reserves and the ancient silk trade route, along with China's diplomatic endeavours in the area, has been
referred to as the "New Great Game." This research centres on the power struggle, considering
geopolitical, geostrategic, and geoeconomic variables. Topics including trade, political hegemony, oil
politics, and conventional and nontraditional security are all explored and explained by the researcher.
Using Mackinder's Heartland, Spykman Rimland, and Hegemonic Stability theories, examines China's role
in Central Asia. This study adheres to the empirical epistemological method and has taken care of
objectivity. This study analyze primary and secondary research documents critically to elaborate role of
china’s geo economic outreach in central Asian countries and its future prospect. China is thriving in trade,
pipeline politics, and winning states, according to this study, thanks to important instruments like the
Shanghai Cooperation Organisation and the Belt and Road Economic Initiative. According to this study,
China is seeing significant success in commerce, pipeline politics, and gaining influence on other
governments. This success may be attributed to the effective utilisation of key tools such as the Shanghai
Cooperation Organisation and the Belt and Road Economic Initiative.
Optimizing Gradle Builds - Gradle DPE Tour Berlin 2024Sinan KOZAK
Sinan from the Delivery Hero mobile infrastructure engineering team shares a deep dive into performance acceleration with Gradle build cache optimizations. Sinan shares their journey into solving complex build-cache problems that affect Gradle builds. By understanding the challenges and solutions found in our journey, we aim to demonstrate the possibilities for faster builds. The case study reveals how overlapping outputs and cache misconfigurations led to significant increases in build times, especially as the project scaled up with numerous modules using Paparazzi tests. The journey from diagnosing to defeating cache issues offers invaluable lessons on maintaining cache integrity without sacrificing functionality.
Advanced control scheme of doubly fed induction generator for wind turbine us...IJECEIAES
This paper describes a speed control device for generating electrical energy on an electricity network based on the doubly fed induction generator (DFIG) used for wind power conversion systems. At first, a double-fed induction generator model was constructed. A control law is formulated to govern the flow of energy between the stator of a DFIG and the energy network using three types of controllers: proportional integral (PI), sliding mode controller (SMC) and second order sliding mode controller (SOSMC). Their different results in terms of power reference tracking, reaction to unexpected speed fluctuations, sensitivity to perturbations, and resilience against machine parameter alterations are compared. MATLAB/Simulink was used to conduct the simulations for the preceding study. Multiple simulations have shown very satisfying results, and the investigations demonstrate the efficacy and power-enhancing capabilities of the suggested control system.
The CBC machine is a common diagnostic tool used by doctors to measure a patient's red blood cell count, white blood cell count and platelet count. The machine uses a small sample of the patient's blood, which is then placed into special tubes and analyzed. The results of the analysis are then displayed on a screen for the doctor to review. The CBC machine is an important tool for diagnosing various conditions, such as anemia, infection and leukemia. It can also help to monitor a patient's response to treatment.
Electric vehicle and photovoltaic advanced roles in enhancing the financial p...IJECEIAES
Climate change's impact on the planet forced the United Nations and governments to promote green energies and electric transportation. The deployments of photovoltaic (PV) and electric vehicle (EV) systems gained stronger momentum due to their numerous advantages over fossil fuel types. The advantages go beyond sustainability to reach financial support and stability. The work in this paper introduces the hybrid system between PV and EV to support industrial and commercial plants. This paper covers the theoretical framework of the proposed hybrid system including the required equation to complete the cost analysis when PV and EV are present. In addition, the proposed design diagram which sets the priorities and requirements of the system is presented. The proposed approach allows setup to advance their power stability, especially during power outages. The presented information supports researchers and plant owners to complete the necessary analysis while promoting the deployment of clean energy. The result of a case study that represents a dairy milk farmer supports the theoretical works and highlights its advanced benefits to existing plants. The short return on investment of the proposed approach supports the paper's novelty approach for the sustainable electrical system. In addition, the proposed system allows for an isolated power setup without the need for a transmission line which enhances the safety of the electrical network
Embedded machine learning-based road conditions and driving behavior monitoringIJECEIAES
Car accident rates have increased in recent years, resulting in losses in human lives, properties, and other financial costs. An embedded machine learning-based system is developed to address this critical issue. The system can monitor road conditions, detect driving patterns, and identify aggressive driving behaviors. The system is based on neural networks trained on a comprehensive dataset of driving events, driving styles, and road conditions. The system effectively detects potential risks and helps mitigate the frequency and impact of accidents. The primary goal is to ensure the safety of drivers and vehicles. Collecting data involved gathering information on three key road events: normal street and normal drive, speed bumps, circular yellow speed bumps, and three aggressive driving actions: sudden start, sudden stop, and sudden entry. The gathered data is processed and analyzed using a machine learning system designed for limited power and memory devices. The developed system resulted in 91.9% accuracy, 93.6% precision, and 92% recall. The achieved inference time on an Arduino Nano 33 BLE Sense with a 32-bit CPU running at 64 MHz is 34 ms and requires 2.6 kB peak RAM and 139.9 kB program flash memory, making it suitable for resource-constrained embedded systems.
1. The primary protection issue is the
fire protection of Class-B external
floating roof liquid storage tanks,
specifically the adequate protection
against potential fire hazards en-
countered in the rim seal area, and
the equipment used to suppress
potential fires caused in conjunc-
tion with this hazard area that meet
the intent of fire safety requirements
as prescribed by the Oil Industry
Safety Directorate (OISD) and Na-
tional Fire Protection Association
Standards NFPA 30 and NFPA 11.
ACAF Systems, Primary Flow Sig-
nal - Fire Suppression Group, LLC
(ACAF Systems) provides a unique
and effective combination of deliv-
ery equipment and fire suppression
agent in one proven package. Due to
the nature of the enhanced system
design and the compressed air foam
(CAF) agent formulation, the fire
suppression equipment and design
proposed do not directly comply
with the prescriptive requirements of
NFPA 30, NFPA 11 Standards for the
floating roof tank rim seal.
Alternatively, NFPA does not restrict
designs to purely singular or a set
of prescribed systems of fire sup-
pression. NFPA documents allow
for the latitude in design and do
recognize that there are always new
technologies and arrangements to
be considered that may potentially
meet fire safety and protection re-
quirements outside the direct scope
as prescribed in the standards. To
this end, NFPA 11, para 1.2.2 states
“Nothing in this standard is intended
to restrict new technologies or al-
ternative arrangements, provided
the level of safety prescribed by the
standard is not lowered.” Thus, al-
lowing for the introduction of new
technologies such as that devel-
oped by ACAF Systems.
FIRE SUPPRESSION
DESIGN
FOR FLOATING ROOK TANK
APPLICATIONS
By Steven E. Younis
Mr. Steven E. Younis is an Independent Professional Fire Protection Engineering
Consultant to ACAF Systems, Primary Flow Signal - Fire Suppression Group, LLC.
www.fs-world.com Spring 2014 edition[ 48 ]
2. NFPA DESIGN
REQUIREMENTS
As specified in NFPA 30, Section
21.6.4, “Fire Control. Tank storage
facilities for flammable and com-
bustible liquids shall be reviewed to
ensure that fire and explosion haz-
ards resulting from lost containment
of liquids are provided with corre-
sponding fire prevention and emer-
gency action plans. (See Section
6.3)” Section 6.3 states the follow-
ing “Management of Fire and Ex-
plosion Hazards. This chapter shall
apply to the management method-
ology used to identify, evaluate, and
control the hazards involved in the
processing and handling of flamma-
ble and combustible liquids. These
hazards include, but are not limited
to, preparation, separation, purifi-
cation and change of state, energy
content or composition.”
On an international level, in com-
pliance with Sections 6.3 and 6.4
(Hazard Analysis) and through the
work of OISD, the hazards have
been identified with regard to float-
ing roof liquid storage tanks, spe-
cifically, the potential fire hazards
within the rim seal area. In order to
protect the rim seal area, in con-
junction with NFPA 30, Section 6.7
(Fire Protection and Fire Suppres-
sion Systems) states “Where the
need is indicated by the hazards of
liquid processing, storage, or ex-
posure as determined by Section
6.4, fixed fire protection shall be
provided.” Subsequently, Section
6.7.6 states “Where provided, fire
control systems shall be designed
and maintained in accordance
with the following NFPA standards,
as applicable: NFPA 11, NFPA 12,
NFPA 12A, NFPA 13, NFPA 15,
NFPA 16, NFPA 17, and NFPA 2001.
In conjunction with the NFPA 30 ref-
erence prescribed above, NFPA 11
is the jurisdictional standard for de-
sign of foam systems for floating roof
tank applications, specifically the
rim seal applications, which are the
concern being addressed. The cur-
rent design requirements for this ap-
plication are covered under NFPA 11.
Section 5.3 (Outdoor Open-Top
Floating Roof Tanks), specifically
Section 5.3.4 (Methods of Seal Fire
Protection). As specified in NFPA 11,
Table 5.3.5.3.6.1, Below-the-Seal
Fixed Foam Discharge Protection
for Open-Top Floating Roof Tanks,
specified that the minimum appli-
cation rate shall be 0.50 gpm/ft2
(20.4 L/min-m2
) with a minimum dis-
charge time of 10 minutes. The ap-
plication rate is based on based on
low expansion foams combined with
delivery equipment that has been
utilized in the market for many years
without significant technology up-
grades.
PROPOSED ACAF SYSTEMS
ALTERNATIVE DESIGN TO
NFPA 11 REQUIREMENTS
ACAF Systems utilizes Solberg RF
foam concentrate as the basis for
the compressed air foam fire sup-
pressant in conjunction with its new
uniquely engineered delivery equip-
ment. CAF is an homogenous foam
produced by the combination of wa-
ter, foam concentrate, and air or ni-
trogen under pressure. A unique fire
fighting foam agent, CAF, extinguish-
es the fire by establishing a blanket
of foam on the flammable liquid sur-
face. The blanket creates separation
of oxygen and heat from the burn-
ing fuel, extinguishing the fire and
preventing re-flash. CAF’s ability to
reduce heat contributes to the effec-
tiveness of this agent. CAF created
with nitrogen provides an even more
effective blanket for superior re-flash
protection as the incorporation of ni-
trogen into the CAF mixture enhanc-
es the fire suppression capabilities
due to its inherent nature as an inert
gas. This combined with the unique,
FM approved ACAF Systems deliv-
ery systems provide for a total pack-
age for effective fire suppression of
Class B hydrocarbon and polar sol-
vent liquid fires similar to those en-
countered in floating roof tank rim
seal applications.
ACAF Systems’ CAF fire suppres-
sion systems are pre-engineered,
special hazard, fire suppression
systems that deliver compressed
air foam through a variety of delivery
systems. The delivery system that
pertains specifically to the rim seal
applications is an automatic fixed
pipe system of specially-designed
nozzles. CAF is created by expand-
ing a foam concentrate RF-3 (for hy-
drocarbon fuels) or alcohol-resistant
AR-AFFF (for polar solvents) foam-
water solutions. The expanded ma-
terial is applied to the hazard area
much the same as foam water sys-
tems are. CAF, however, has many
distinct properties that need to be
considered in the design and instal-
lation of a system. How the CAF is
created and discharged is an impor-
tant aspect of the design; as such,
special nozzles are used to distribute
the CAF over a hazard area. It extin-
guishes the fire threat through the
following combination of processes:
1. Excludes air from the flammable
vapors.
2. Eliminates vapor release from
fuel surface.
3. Separates the flames from the
fuel surface.
4. Cools the fuel surface and sur-
rounding structural surfaces.
Hazards that CAF systems are per-
mitted to protect include the following:
1. Flammable liquids (flash points
below 38°C (100°F) having a
vapor pressure not exceeding
276 KPa (40 psi).
2. Combustible liquids (flash point
of 38°C (100°F) and above).
ACAF Systems are suitable for
Class B hydrocarbon and polar
solvents flammable liquids, stor-
age and handling locations where
the risk of spill and pool fires exist.
Note, polar solvents are liquids that
have high dielectric constants, are
chemically active, and form coordi-
nate covalent bonds; examples are
alcohols and ketones - methanol,
ethanol, propanol, formic acid, ethyl
acetate, acetonitrile, etc.
The ACAF Systems rim seal sys-
tems components that have been
proposed for protection are fully
tested and evaluated and have
received FM Approvals for the
meeting and/or exceeding the re-
quirements of extinguishing and
suppressing hydrocarbon and po-
lar solvent fires as prescribed. The
system utilizes Solberg RE-HEAL-
ING Foam Concentrate in 6% con-
centration. When utilized with the
unique CAF delivery equipment,
the CAF is delivered to the fire
at a 13 to 1 expansion ratio. With
the receipt of FM Approvals, the
equipment meets the requirement
set forth in NFPA 11, under the
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3. general requirements for System
Components and System Types,
Chapter 4, NFPA 11, para 4.1.1 “All
components shall be listed for their
intended use.” As a note, NFPA
defines listed as follows “Equip-
ment, materials, or services in a
list published by an organization
that is acceptable to the authority
having jurisdiction and concerned
with evaluation of products and
services, that maintains periodic
inspection of production of listed
equipment, materials or periodic
evaluation of services, and whose
listing states that either the equip-
ment material, or service meets ap-
propriate designated standards or
has been tested and found suitable
for a specified purpose.” FM is a
recognized authority and leader in
testing, evaluation, and approval of
such products, materials, and ser-
vices. It shall be noted that FM has
no approval standard for rim seal
protection systems.
Through the testing, evaluation,
and approval process specified
above, the systems have received
approvals for use to extinguish
Class B hydrocarbon and polar
solvent fuel fires. Specific to the
rim seal application, the systems
are designed as a total flood foam
extinguishing system with the abil-
ity to extinguish Class B hydro-
carbon and polar solvent fuel fires
with an application rate of 12.4 L/
min-m2
(0.3 gpm/ft2
), a rate of ap-
plication that is seven times greater
than the FM approved ROA for hy-
drocarbons. The variation from the
NFPA 11 requirements is that the
discharge will not continue for 10
minutes as required, it will com-
pletely discharge and entirely fill
the rim seal void space in approxi-
mately 1.5 minutes, therefore not
requiring the extended discharge.
The design is intended to provide a
total flood of the rim seal space this
is due to the characteristics of the
CAF specifically its 13 to 1 expan-
sion ratio combined with its ability
to hold 25% draintime for greater
than 1.5 hours. The CAF will re-
main place in a stable state that
will not break down significantly
enough to allow reflash of the fire.
The agent is of high integrity and
will not break down. This has been
proven through testing. These
characteristics support the use of
the compressed air foam as a to-
tal flooding extinguishing agent for
this application and should support
it approval for use above prescrip-
tive requirements.
ACAF Systems has developed a
design for installation of the CAF
fire protection system that meets
the parameters of NFPA 11 with a
rate of application of 20.4 L/min-
m2
(0.50 gpm/ft2
). This, according
to NFPA 11, is the recommended
level of protection that will protect
against the incident of the poten-
tial hydrocarbon and polar solvent
fuel fires that may occur within the
rim seal application on the float-
ing roof liquid storage tanks. The
delivery system combined with the
CAF formulation has significantly
increased the fire suppression ca-
pability of the foam system over the
long used equipment of the past
decades. The detection and alarm
system will be cross-zoned and
consist of approved, listed com-
ponents per requirements of NFPA
standards. Also of note, that with
the achievement of gaining FM Ap-
provals, the systems have also met
or exceeded the requirements of
UL 162, UL Standard for Safety of
Foam Equipment and Liquid Con-
centrates.
OISD REVIEW AND
APPROVAL
As previously stated, under the
parameters of NFPA 11, para
1.2.2, an authority having ju-
risdiction, in this case OISD,
has the option after review and
evaluation, to provide approval
based on the facts presented,
to approve the use of ACAF
Systems CAF systems to pro-
tect the rim seal area of floating
roof liquid storage tanks against
Class B hydrocarbon fuel and
polar solvent based fires. ACAF
Systems submitted schematic
design and performance data
to OISD for review and approval
use in rim seal fire suppression
applications. OISD performed
a comprehensive review of the
submission, and upon comple-
tion of final qualification testing
may grant final approvals for ACAF
Systems’ design with regard to
floating tank rim seal applications.
PERFORMANCE SUMMARY
In conclusion, ACAF Systems rim
seal fire suppression provides the
following advantages over older
more dated technologies:
• Utilizes an environmentally-safe
foam that is fluorine free
• Significantly increased expansion
ratio than currently used foams,
on the order of 13 to 1
• Due to the internal structure of the
CAF, there is greater reflash pro-
tection
• The CAF provides total flooding
characteristics to fill the rim seal
space completely
• Greater drain time, which equates
to slower breakdown and longer
lasting foam
• Reduced hardware requirements
• Centralized control equipment
translating into greater reliability
and reduced life cycle costs
• All control valves, solution levels,
and nitrogen pressure are moni-
tored to minimize failure modes
and maintain optimal perfor-
mance condition
• Electric / pneumatic release sys-
tems
• Manufactured and installed with
stainless steel piping systems for
longer service life
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