This document provides information about LPG (liquefied petroleum gas) and gas detection systems. It discusses what LPG is, how it is used to supply buildings and various appliances, and the components of LPG and gas detection systems including piping, outlets, sensors, panels, and standards. The document also outlines procedures for installing, testing, commissioning, maintaining and operating LPG and gas detection systems. Calculations for LPG demand, storage, and pipe sizing are presented.
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1. Sprinkler system Type
WET PIPE SPRINKLER SYSTEM
DRY PIPE SPRINKLER SYSTEM
PRE-ACTION SYSTEM
DELUGE SYSTEM
WET PIPE ANTI FREEZE SYSTEM
FOAM WATER SPRINKLER SYSTEM
2. Sprinkler Selection
3 . Piping
4. Hydraulic Calculation
5. Standpipe System
6. Pump Selection & Types
PREMIUM BOOK WITH HIGH DEFINITION QUALITY.
**A complete Guide of Fire fighting System.**
This HANDBOOK has been made from references of many books from all over the world. Which has been collected in one book.
1. Sprinkler system Type
WET PIPE SPRINKLER SYSTEM
DRY PIPE SPRINKLER SYSTEM
PRE-ACTION SYSTEM
DELUGE SYSTEM
WET PIPE ANTI FREEZE SYSTEM
FOAM WATER SPRINKLER SYSTEM
2. Sprinkler Selection
3 . Piping
4. Hydraulic Calculation
5. Standpipe System
6. Pump Selection & Types
Fundamental training on Fire Detection & Alarm SystemSabrul Jamil
This is a basic training on Fire Detection and Alarm System, created to give my colleagues from non-engineering divisions a comprehensive brief on the system. This is most suitable for individuals with little or no technical knowledge. This training introduces the devices and the system in a whole, not how to design it.
Brief introduction to Fired Heaters operation and design. Definition of the different Heaters in the industry and brief strategy how to operate them safely.
1. Sprinkler system Type
WET PIPE SPRINKLER SYSTEM
DRY PIPE SPRINKLER SYSTEM
PRE-ACTION SYSTEM
DELUGE SYSTEM
WET PIPE ANTI FREEZE SYSTEM
FOAM WATER SPRINKLER SYSTEM
2. Sprinkler Selection
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Fire and Gas Detection System : Part 2_Block Diagram_Philosophy, Signal Types...Gan Chun Chet
Fire and Gas Detection System Requirements for the Oil and Gas Industry. Offshore Platforms are also applicable for onshore plants/terminals. Safeguarding and Protective System to ensure oil and gas facilities are safe to operate.
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Latest T4S guidelines for storage, handling and dispensing of CNG at mother station, online station and daughter booster station.
This presentation make it simple and understandable to the guidelines for setting up of the layout for CNG station including, inter distance between various equipment and units, storage guidelines, filling guidelines and safety guidelines.
I have try to cover all the safety requirements of various equipment to be installed at a CNG station for its storage and dispensing.
OISD-STD-117 Fire Protection Facilities for Petroleum Depots, Terminals, Pipe...AnupamaPanoli
OISD (Oil Industry Safety Directorate) is a technical directorate under the Ministry of Petroleum and Natural Gas that formulates and coordinates the implementation of a series of self regulatory measures aimed at enhancing the safety in the oil & gas industry in India.
It is intended that the provisions specified in this standard shall be implemented progressively for the existing facilities. For the new / upcoming locations / facilities, these shall be implemented along with commissioning.
This standard recommends the minimum requirement of fire protection facilities at Petroleum Depots, Terminals, Pipeline Installations with or without Storages, Central Tank Farms (CTF), Lube Oil Installations, Grease Manufacturing & Filling Facilities.
Fundamental training on Fire Detection & Alarm SystemSabrul Jamil
This is a basic training on Fire Detection and Alarm System, created to give my colleagues from non-engineering divisions a comprehensive brief on the system. This is most suitable for individuals with little or no technical knowledge. This training introduces the devices and the system in a whole, not how to design it.
Brief introduction to Fired Heaters operation and design. Definition of the different Heaters in the industry and brief strategy how to operate them safely.
1. Sprinkler system Type
WET PIPE SPRINKLER SYSTEM
DRY PIPE SPRINKLER SYSTEM
PRE-ACTION SYSTEM
DELUGE SYSTEM
WET PIPE ANTI FREEZE SYSTEM
FOAM WATER SPRINKLER SYSTEM
2. Sprinkler Selection
For COMPLETE PREMIUM BOOK PLZZ
Check out my product on Instamojo:https://www.instamojo.com/ezazsidd1993/fire-fighting-a-complete-handbook/
Fire and Gas Detection System : Part 2_Block Diagram_Philosophy, Signal Types...Gan Chun Chet
Fire and Gas Detection System Requirements for the Oil and Gas Industry. Offshore Platforms are also applicable for onshore plants/terminals. Safeguarding and Protective System to ensure oil and gas facilities are safe to operate.
Guidelines for storage Handling and Dispensing of CNG.pptxAbhishek Padiyar
Latest T4S guidelines for storage, handling and dispensing of CNG at mother station, online station and daughter booster station.
This presentation make it simple and understandable to the guidelines for setting up of the layout for CNG station including, inter distance between various equipment and units, storage guidelines, filling guidelines and safety guidelines.
I have try to cover all the safety requirements of various equipment to be installed at a CNG station for its storage and dispensing.
OISD-STD-117 Fire Protection Facilities for Petroleum Depots, Terminals, Pipe...AnupamaPanoli
OISD (Oil Industry Safety Directorate) is a technical directorate under the Ministry of Petroleum and Natural Gas that formulates and coordinates the implementation of a series of self regulatory measures aimed at enhancing the safety in the oil & gas industry in India.
It is intended that the provisions specified in this standard shall be implemented progressively for the existing facilities. For the new / upcoming locations / facilities, these shall be implemented along with commissioning.
This standard recommends the minimum requirement of fire protection facilities at Petroleum Depots, Terminals, Pipeline Installations with or without Storages, Central Tank Farms (CTF), Lube Oil Installations, Grease Manufacturing & Filling Facilities.
Smart Automation Gas Level Monitoring with Gas Leakage Deduction and Refill B...ijtsrd
The main aim of this project is to monitor forliquefied petroleum gas (LPG) leakage to avoid fireaccidents providing house safety feature where securityhas been an important issue. The most commonproblem experienced in our day- to- day lives that isregarding GAS leakage system. When it comes it tosafety of the surrounding as well as gas container wehave an MQ-5(gas sensor), which will detect the gasesby propane, butane, carbon monoxide ,smoke ,alcoholetc. The system detects the leakage of LPG using gassensor and When the system detects the LPGconcentration in the air exceeds the certain level then itimmediately takes action by automatically. Thus herewe are using the gas sensor which placed in the leakpoints, which senses the concentration value of gasessuch as propane ,butane ,smoke ,alcohol , carbon monooxideetc and when the concentration value exceeds thenormal value the leakage of gas is detected , and alertsystem used by buzzer and the automatically open thewindows prevent fire accidents. The gas sensor hasbeen used which has high sensitivity to gases likepropane and butane. When the concentration of LPG inair exceeds a certain level, the sensor senses the gasleakage and the output of the sensor goes LOW. Thedetection is done by the gas sensor, through themicro controller the LED and buzzer are turned ONsimultaneously. Using relay DC motor is automaticallyopen the windows. Prof. M. Joe Marshell | S. Shanthini"Smart Automation Gas Level Monitoring with Gas Leakage Deduction and Refill Booking using Embedded System" Published in International Journal of Trend in Scientific Research and Development (ijtsrd), ISSN: 2456-6470, Volume-1 | Issue-6 , October 2017, URL: http://www.ijtsrd.com/papers/ijtsrd4666.pdf http://www.ijtsrd.com/engineering/gas-engineering/4666/smart-automation-gas-level-monitoring-with-gas-leakage-deduction-and-refill-booking-using-embedded-system/prof-m-joe-marshell
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V 1 presentation on safety aspects of lpg handling and storageImran Bokhari
Liquefied Petroleum Gas (LPG) is a mixture of Propane and Butanes, with Propane content of 30 to 60 percent and Butanes content of 40 to 70 percent. LPG can exist in liquid state at moderate pressure at ambient temperature. It is colorless, odorless, highly volatile and heavier than air (even at ambient conditions) substance. It easily forms combustible/explosive mixture when released in air, thus posing unique safety issues. Besides being a combustible substance posing fire hazard, LPG due to its nature also poses threats of cold burns and suffocation. LPG is being extensively used as fuel in homes, restaurants, transportation and some industries. In this presentation we have discussed in detail a major HSE related incident that have occurred in the past and mitigation strategies for the same. The required safety devices and their engineering design features in LPG extraction plant to avoid accidents are also discussed.
Immunizing Image Classifiers Against Localized Adversary Attacksgerogepatton
This paper addresses the vulnerability of deep learning models, particularly convolutional neural networks
(CNN)s, to adversarial attacks and presents a proactive training technique designed to counter them. We
introduce a novel volumization algorithm, which transforms 2D images into 3D volumetric representations.
When combined with 3D convolution and deep curriculum learning optimization (CLO), itsignificantly improves
the immunity of models against localized universal attacks by up to 40%. We evaluate our proposed approach
using contemporary CNN architectures and the modified Canadian Institute for Advanced Research (CIFAR-10
and CIFAR-100) and ImageNet Large Scale Visual Recognition Challenge (ILSVRC12) datasets, showcasing
accuracy improvements over previous techniques. The results indicate that the combination of the volumetric
input and curriculum learning holds significant promise for mitigating adversarial attacks without necessitating
adversary training.
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Water billing management system project report.pdfKamal Acharya
Our project entitled “Water Billing Management System” aims is to generate Water bill with all the charges and penalty. Manual system that is employed is extremely laborious and quite inadequate. It only makes the process more difficult and hard.
The aim of our project is to develop a system that is meant to partially computerize the work performed in the Water Board like generating monthly Water bill, record of consuming unit of water, store record of the customer and previous unpaid record.
We used HTML/PHP as front end and MYSQL as back end for developing our project. HTML is primarily a visual design environment. We can create a android application by designing the form and that make up the user interface. Adding android application code to the form and the objects such as buttons and text boxes on them and adding any required support code in additional modular.
MySQL is free open source database that facilitates the effective management of the databases by connecting them to the software. It is a stable ,reliable and the powerful solution with the advanced features and advantages which are as follows: Data Security.MySQL is free open source database that facilitates the effective management of the databases by connecting them to the software.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
Harnessing WebAssembly for Real-time Stateless Streaming PipelinesChristina Lin
Traditionally, dealing with real-time data pipelines has involved significant overhead, even for straightforward tasks like data transformation or masking. However, in this talk, we’ll venture into the dynamic realm of WebAssembly (WASM) and discover how it can revolutionize the creation of stateless streaming pipelines within a Kafka (Redpanda) broker. These pipelines are adept at managing low-latency, high-data-volume scenarios.
Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
In this month's edition, along with this month's industry news to celebrate the 13 years since the group was created we have articles including
A case study of the used of Advanced Process Control at the Wastewater Treatment works at Lleida in Spain
A look back on an article on smart wastewater networks in order to see how the industry has measured up in the interim around the adoption of Digital Transformation in the Water Industry.
Student information management system project report ii.pdfKamal Acharya
Our project explains about the student management. This project mainly explains the various actions related to student details. This project shows some ease in adding, editing and deleting the student details. It also provides a less time consuming process for viewing, adding, editing and deleting the marks of the students.
NUMERICAL SIMULATIONS OF HEAT AND MASS TRANSFER IN CONDENSING HEAT EXCHANGERS...ssuser7dcef0
Power plants release a large amount of water vapor into the
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as sensible heat due to lowering the flue gas exit temperature.
Additionally, harmful acids released from the stack can be
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Condensation of vapors in flue gas is a complicated
phenomenon since heat and mass transfer of water vapor and
various acids simultaneously occur in the presence of noncondensable
gases such as nitrogen and oxygen. Design of a
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condensation in a flue gas condensing heat exchanger was
developed using MATLAB. Governing equations based on
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predict variables such as flue gas exit temperature, cooling
water outlet temperature, mole fraction and condensation rates
of water and sulfuric acid vapors. The equations were solved
using an iterative solution technique with calculations of heat
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LPG – Liquefied Petroleum Gas & Gas Detection System
1. LPG – Liquefied Petroleum Gas
& Gas Detection System
– LPG & Gas Detection System,
Installation, Testing & Commissioning,
design, Calculation.
Prepared By: Monzer Salahdine
2. Introduction
LPG System used to supply :
LPG: Liquefied Petroleum Gas
I. Building – residential – kitchens.
II. Restaurants, industrial kitchens.
III. Laboratories, medical collages.
IV. Boilers.
V. Cars.
3. Introduction
LPG, Gas detection Systems:
I. LPG – Mechanical: Piping, Solenoid, Outlets.
II. Gas Detection System, Sensors, Panels.
LPG, Code and Standards:
1. NFPA 58: Liquefied Petroleum Gas Code.
4. Schematic Module
PIPES ASSETS
LPG & Gas Detection System as below procedure:
TESTING &
COMMISSIONING
MAINTENANCE
& OPERATION
MaintenanceInstallation & Commissioning
5. Introduction
What is LPG:
A - Liquefied petroleum gas or liquid petroleum gas (LPG or LP gas), also referred to as simply
propane or butane, is a flammable mixture of hydrocarbon gases used as a fuel in heating appliances,
cooking equipment, and vehicles.
B - Varieties of LPG bought and sold include mixes that are primarily propane (C3H8), primarily
butane (C4H10) and, most commonly, mixes including both propane and butane.
C - LPG has a typical specific calorific value of 46.1 MJ/kg compared with 42.5 MJ/kg for fuel oil and
43.5 MJ/kg for premium grade petrol (gasoline). However, its energy density per volume unit of 26
MJ/L is lower than either that of petrol or fuel oil, as its relative density is lower (about 0.5–0.58,
compared to 0.71–0.77 for gasoline).
6. Introduction
What is LPG:
D - As its boiling point is below room temperature, LPG will evaporate quickly at normal
temperatures and pressures and is usually supplied in pressurized steel vessels. They are typically filled
to 80–85% of their capacity to allow for thermal expansion of the contained liquid. The ratio between
the volumes of the vaporized gas and the liquefied gas varies depending on composition, pressure, and
temperature, but is typically around 250:1. The pressure at which LPG becomes liquid, called its vapor
pressure, likewise varies depending on composition and temperature; for example, it is approximately
220 kilopascals (32 psi) for pure butane at 20 °C (68 °F), and approximately 2,200 kilopascals (320 psi)
for pure propane at 55 °C (131 °F). LPG is heavier than air, unlike natural gas, and thus will flow
along floors and tend to settle in low spots, such as basements. There are two main dangers from this.
The first is a possible explosion if the mixture of LPG and air is within the explosive limits and there is
an ignition source. The second is suffocation due to LPG displacing air, causing a decrease in oxygen
concentration.
E - Commercially available LPG is currently derived from fossil fuels. Burning LPG releases carbon
dioxide, a greenhouse gas. The reaction also produces some carbon monoxide. LPG does, however,
release less CO, 2 per unit of energy than does coal or oil. It emits 81% of the CO
2 per kWh produced by oil, 70% of that of coal, and less than 50% of that emitted by coal-generated
electricity distributed via the grid. Being a mix of propane and butane, LPG emits less carbon per joule
than butane but more carbon per joule than propane.
7. Introduction
Odor Of LPG:
In their natural state, LPG (Propane and Butane) and Natural Gas
(Methane) are all odorless gases. The distinctive smell that people
associate with these gases is actually added to them as a safety
measure.
For many decades, the gaseous fuels industry has added odorants to
LPG and Natural Gas so that people can detect gas leaks with nothing
more than their noses. Without the addition of an odorant, leaking
gas could collect without being detected. This would create a
dangerous condition that could lead to an explosion or fire.
8. Introduction
LPG – schematic – residential example:
Gas Detector Of LPG at low level ( LPG heavier than
air).
Gas Detector Of Natural Gas and Coal gas at High
level (Air heavier than Natural Gas & Coal Gas).
10. Training Module
In case of gas leakage inside the area (Kitchen, Lab), the gas sensor will
be activated.
When sensor activated, it will send a signal to the control panel which
will treat it as leakage inside the lab.
The panel will give signal to the solenoid valve to close immediately
(safety issue) to make sure no more gas flow to the area.
The panel will give another signal to the siren light (alarm, mean there
is leakage).
The panel will give signal to fire alarm system which will deactivate the
main solenoid valve of LPG of entire building(safety issue).
The panel will give signal to BMS system to notify to the operator
(maintenance team) that there is a gas leakage.
The operator (maintenance team) has to check if there is leakage or any
of outlet open and to close it immediately.
When make sure that no more gas leakage inside the lab, the operator
to make reset for the panel which will activate the system and the gas
flow inside the lab, and to reset the solenoid manually.
In case of fire alarm in the building, the main solenoid will be shut off
(safety issue), once signal not disappear the system will be automatic ally.
11. Schematic Module
LPG Station
Main LPG panel, including solenoid and
regulator( up to 20 PSI) Solenoid Valve
SUB LPG Panel
Outlets
Including Solenoid
& Regulator( up to
5 PSI)
Liquid Gas
6.9 Bars
5 PSI
Outlets
1.5 to 2.5 PSI
10-20 PSI
13. Pipes
Pipes for LPG: black steel seamless SCH80, galvanized steel,
polyethylene (under ground) Or Copper Pipes Type K & L:
Black steel Pipes – seamless SCH 80, threaded
installed in double containment pipes for protection
or welding without double containment.
Copper Pipes Brazing and threaded for the fittings
( valves, Outlets).
14. Solenoid Valve
It is electrical control valve energized from
control panel to shut off the gas in case there is
leakage.
Solenoid valve is normally close, once the panel
energized the panel send signal to solenoid to
open.
In case there is leakage, the panel cut the power
to solenoid and became again closed ( solenoid
Spring Type).
15. Detector
Detectors for LPG SENSITROM brand or other.
Detectors installed at low level at 30 cm from finish floor level
and above ceiling in double containment or near the welding
joint,
Detector detect the LPG leakage and give signal to detection
control panel.
This sensor module utilizes an MQ-6 as the sensitive
component and has a protection resistor and an adjustable
resistor on board. The MQ-6 gas sensor is highly sensitive to
LPG, iso-butane, propane and less sensitive to alcohol,
cooking fume and cigarette smoke. It could be used in gas
leakage detecting equipment in family and industry. The
resistance of the sensitive component changes as the
concentration of the target gas changes.
Each detector will have an IP and address where all detectors
will be labeled and reflected the same label in LPG detection
panel- in case of leakage will knowing which detector giving
the signal and the location of each.
16. SIREN LIGHT
SIREN light for LPG SENSITROM
brand or other.
Once LPG system is activated, panel will
give signal to siren light to alert the area
about the LPG leakage( Visio and
Audio).
Wall mounted or ceiling mounted.
17. Detection Control Panel
Detection control panel for LPG SENSITROM brand or other.
When sensor level reach more than 10, alarm 1 will be activated( solenoid level
close but no alarm).
When sensor level reach more than 15, alarm 2 will be activated( solenoid
close, alarm occur).
Once sensor level reach more than 20 , alarm 3 will be activated ( solenoid
close, alarm occur, given alarm to fire alarm and BMS).
18. LPG Gas Panel
Ball Valve
Strainer
Solenoid Valve
Gas detector
Gas regulator
Pressure Gauge
Ball Valve
Gas Relief
19. Testing & Commissioning
The LPG system tested and certified by Third Party-
specialist in installation and commissioning of LPG system
and certified from NFPA58.
Below tools used for the tests:
20. Testing & Commissioning
Test Procedures:
The testing commissioning of LPG system follow the below
procedure:
1) Leak test( all pipes are tested by nitrogen for leak test).
2) Flushing( all pipes flushed by compressed air and nitrogen
to clean them from particles and humidity.
3) Cross test(valve test- when valve close, gases not allow to
reach to others connections.
4) Flow test.
5) Final leak test once open the LPG, testing by manual LPG
detector sensor.
21. Testing & Commissioning
Why we make the above test ??
Targets and goals of LPG tests:
1. To maintain the equipments life and saving
money.
2. To reduce the risk (avoid LPG leakages in
future).
3. Maintenance team to inspect and check in
daily basis to maintain the above two items
(check list).
22. Precautions & Recommendations
1. Once LPG detector detect a gas leakage,
system will be alert, all persons should leave
the room immediately.
2. Specialist of LPG system (maintenance
company) should investigate the cause of
leakage and rectify if any than to reset and re
open the LPG system.
3. Maintenance company to make a check list
for each panel in daily basis.
4. Damages pieces or sensors to be rectified
immediately to maintain secured areas.
25. Design & Calculation
Storage Calculation:
a.) Estimate No. of Lpg outlets
1. FOUR GAS BURNER RANGE ON GAS OVEN = 1 OUTLET
2. GAS POT STOVE ON STAND = 1 OUTLETS
3. SMOOTH PLATE GAS GRIDDLE = 0 OUTLET
4.GAS BIOLING PAN = 0 OUTLET
5. BOWEL GAS FRYER = 0 OUTLET
b.) Design Datas:
1. 4 BURNER OVEN = 65,000 Btu/Hr
2. GAS POT STOVE ON STAND = 40,000 Btu/Hr
3. SMOOTH PLATE GAS GRIDDLE = 30,000 Btu/Hr
4.GAS BIOLING PAN = 30,000 Btu/Hr
5. BOWEL GAS FRYER = 30,000 Btu/Hr
TOTAL = 105,000 Btu/Hr
c.) Calculation of Lpg consumption/day:
3. LPG HEATING VALUE AFTER VAPORIZATION = 2,500 Btu/h/Ft³ FROM ASPE
4. SIMULTANEOUS USE FACTOR ( PEAK HOUR AT LUNCH ONLY ) = 60%
5. ASSUMED BURNER WORKING TIME = 6 Hrs./Day
( 2 hrs per meal serve)
TOTAL LPG CONSUMPTION PER DAY = 151 Ft³
CONVERTING CU FT OF VAPOR TO GALLONS (75 ft3 / 36.39) = 4 G/Day
USE STORAGE TANK FOR ONE WEEK = 110 L
26. Design & Calculation
Pipe Size – Steel Pipe Sch40:
LPG pipes size depend to the
following:
- Pressure inside the pipe.
- Pipe lengths.
Btu/h or KW will be reduced with
pipe length ( otherwise pipe size to
be increased – see below).