Piping & Instrumentation Diagrams
Basic Piping & Instrumentation Diagrams PDF
Presented by: Tejas D. Deshpande
Usually dispatched in 2 to 3 days
Usually dispatched in 2 to 3 days
Category:
Hydraulic , Piping & Fittings
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Pipe Inspection Manual
The New Zealand Pipe Inspection Manual 3rd Edition has been prepared in order to provide:
• An overview of the tasks that can be completed using Closed Circuit Television (CCTV) and how these activities can be used to manage wastewater and stormwater assets.
• A standardised set of codes for recording observations noted during CCTV inspections.
• An outline of good practice procedures for carrying out CCTV inspections and for processing and analysing the information collected.
• Standard Technical Specifications and Model Conditions of Contract for use when engaging CCTV contractors.
Pipe Inspection Manual
The New Zealand Pipe Inspection Manual 3rd Edition has been prepared in order to provide:
• An overview of the tasks that can be completed using Closed Circuit Television (CCTV) and how these activities can be used to manage wastewater and stormwater assets.
• A standardised set of codes for recording observations noted during CCTV inspections.
• An outline of good practice procedures for carrying out CCTV inspections and for processing and analysing the information collected.
• Standard Technical Specifications and Model Conditions of Contract for use when engaging CCTV contractors.
Pipe Flow-Friction Factor Calculations with Excel, Course
Several kinds of pipe flow calculations can be made with the Darcy- Weisbach equation and the Moody friction factor. These calculations can be conveniently carried out with an Excel spreadsheet. Many of the calculations require an iterative solution, so they are especially suitable for an Excel spreadsheet solution. This course includes discussion of the Darcy- Weisbach equation and the parameters in the equation along with the U.S.
and S.I. units to be used. Example calculations and sample Excel spreadsheets for making the calculations are also included. This course is intended primarily for civil engineers, mechanical engineers, chemical engineers, and environmental engineers. After completing this course you will be able to make calculations with the Darcy Weisbach equation and the Moody friction factor equations to calculate several different unknown parameters when sufficient input data is provided. You will also be prepared to use Excel spreadsheets to efficiently make the calculations.
Pipe Flow-Friction Factor Calculations with Excel, Course
Several kinds of pipe flow calculations can be made with the Darcy- Weisbach equation and the Moody friction factor. These calculations can be conveniently carried out with an Excel spreadsheet. Many of the calculations require an iterative solution, so they are especially suitable for an Excel spreadsheet solution. This course includes discussion of the Darcy- Weisbach equation and the parameters in the equation along with the U.S.
and S.I. units to be used. Example calculations and sample Excel spreadsheets for making the calculations are also included. This course is intended primarily for civil engineers, mechanical engineers, chemical engineers, and environmental engineers. After completing this course you will be able to make calculations with the Darcy Weisbach equation and the Moody friction factor equations to calculate several different unknown parameters when sufficient input data is provided. You will also be prepared to use Excel spreadsheets to efficiently make the calculations.
Difficult to Pig Pipelines
Pigging : A widely utilized process which is the act of propelling a properly sized spherical or cylindrical device through the interior of a pipeline by manipulating the pressure & flow of the existing media, or by artificially introduced media or by mechanically pulling the device through the pipeline for the
specific purpose of cleaning, inspecting or distributing inhibitor throughout the pipeline.
Difficult to Pig Pipelines
Pigging : A widely utilized process which is the act of propelling a properly sized spherical or cylindrical device through the interior of a pipeline by manipulating the pressure & flow of the existing media, or by artificially introduced media or by mechanically pulling the device through the pipeline for the
specific purpose of cleaning, inspecting or distributing inhibitor throughout the pipeline.
Basic Pipe Stress Analysis Tutorial
It is common practice worldwide for piping designers to route piping by considering mainly space, process and flow constraints (such as pressure drop) and other requirements arising from constructability, operability and reparability. Unfortunately, pipe stress analysis requirements are often not sufficiently considered while routing and supporting piping systems, especially in providing adequate flexibility to absorb expansion/contraction of pipes due to thermal loads. So, when “as designed” piping systems are handed-off to pipe stress engineers for detailed analysis, they soon realize that the systems are “stiff” and suggest routing changes to make the systems more flexible. The piping designers, in turn, make changes to routing and send the revised layout to the pipe stress engineers to check for compliance again. Such “back and forth” design iterations between layout and stress departments continue until a suitable layout and support scheme is arrived at, resulting in significant increase in project execution time, which, in turn, increases project costs. This delay in project execution is further worsened in recent years by increased operating pressures and temperatures in order to increase plant output; increased operating pressures increase pipe wall thicknesses, which, in turn, increase piping stiffnesses further. Such increased operating temperatures applied on “stiffer” systems increase pipe thermal stresses and support loads. So, it is all the more important to make the piping layout flexible at the time of routing.
Basic Pipe Stress Analysis Tutorial
It is common practice worldwide for piping designers to route piping by considering mainly space, process and flow constraints (such as pressure drop) and other requirements arising from constructability, operability and reparability. Unfortunately, pipe stress analysis requirements are often not sufficiently considered while routing and supporting piping systems, especially in providing adequate flexibility to absorb expansion/contraction of pipes due to thermal loads. So, when “as designed” piping systems are handed-off to pipe stress engineers for detailed analysis, they soon realize that the systems are “stiff” and suggest routing changes to make the systems more flexible. The piping designers, in turn, make changes to routing and send the revised layout to the pipe stress engineers to check for compliance again. Such “back and forth” design iterations between layout and stress departments continue until a suitable layout and support scheme is arrived at, resulting in significant increase in project execution time, which, in turn, increases project costs. This delay in project execution is further worsened in recent years by increased operating pressures and temperatures in order to increase plant output; increased operating pressures increase pipe wall thicknesses, which, in turn, increase piping stiffnesses further. Such increased operating temperatures applied on “stiffer” systems increase pipe thermal stresses and support loads. So, it is all the more important to make the piping layout flexible at the time of routing.
Considerations in the Hydraulic Design of Pipelines
The report summarises the findings of pipe reviews which were conducted during the research project
and highlights the following actions which should be considered during the hydraulic design of
pipelines :
• Review and incorporate available recorded hydraulic performance data of pipelines in the region in the design of new infrastructure;
• Include the secondary energy loss associated with the dimensional details of the couplings in the calculation of the energy loss in the pipeline;
• Use the proposed BRM (biofilm resistance model) to calculate a representative roughness for biofouled pipelines;
• Implement the proposed procedure to determine the remaining useful life of pipelines to be able to prioritize the upgrading or replacement of system components; and
• Provide monitoring points for the initial, continuous or intermittent hydraulic assessment of the pipeline.
Considerations in the Hydraulic Design of Pipelines
The report summarises the findings of pipe reviews which were conducted during the research project
and highlights the following actions which should be considered during the hydraulic design of
pipelines :
• Review and incorporate available recorded hydraulic performance data of pipelines in the region in the design of new infrastructure;
• Include the secondary energy loss associated with the dimensional details of the couplings in the calculation of the energy loss in the pipeline;
• Use the proposed BRM (biofilm resistance model) to calculate a representative roughness for biofouled pipelines;
• Implement the proposed procedure to determine the remaining useful life of pipelines to be able to prioritize the upgrading or replacement of system components; and
• Provide monitoring points for the initial, continuous or intermittent hydraulic assessment of the pipeline.
Hydraulic Study For The New Cairo Raw Water Pipeline
phase is expected to be completed by the end of 2011. The system consists of one raw water intake pump station (IPS), three booster pump stations (BPS 2, 3, and 4), and multiple parallel 2200-millimeter (mm) and 2600-mm diameter pipelines that run approximately 30 kilometers (km) from the Nile River to the newly constructed New Cairo Potable Water Treatment Plant (WTP). Construction will be completed in eight pump installation phases, with design flows ranging from 6 cubic meters per second (m3/sec) at Phase 1 to an ultimate flow of 48 m3 Because the pumping capacity required for Phases 5-8 is to be supplied by a parallel system of pump stations and pipelines that mirror Phases 1-4 (with identical hydraulics and capacities), the following report is based on analysis of Phases 1-4 only. The ultimate flow rate for Phase 4 is 24 m /sec at Phase 8.
Hydraulic Study For The New Cairo Raw Water Pipeline
phase is expected to be completed by the end of 2011. The system consists of one raw water intake pump station (IPS), three booster pump stations (BPS 2, 3, and 4), and multiple parallel 2200-millimeter (mm) and 2600-mm diameter pipelines that run approximately 30 kilometers (km) from the Nile River to the newly constructed New Cairo Potable Water Treatment Plant (WTP). Construction will be completed in eight pump installation phases, with design flows ranging from 6 cubic meters per second (m3/sec) at Phase 1 to an ultimate flow of 48 m3 Because the pumping capacity required for Phases 5-8 is to be supplied by a parallel system of pump stations and pipelines that mirror Phases 1-4 (with identical hydraulics and capacities), the following report is based on analysis of Phases 1-4 only. The ultimate flow rate for Phase 4 is 24 m /sec at Phase 8.
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