In this article, you learn how to create, publish, run, and track a machine learning pipeline by using the Azure Machine Learning SDK. Use ML pipelines to create a workflow that stitches together various ML phases, and then publish that pipeline into your Azure Machine Learning workspace to access later or share with others. ML pipelines are ideal for batch scoring scenarios, using various computes, reusing steps instead of rerunning them, as well as sharing ML workflows with others. Compare these different pipelines. Each phase of an ML pipeline, such as data preparation and model training, can include one or more steps. ML pipelines use remote compute targets for computation and the storage of the intermediate and final data associated with that pipeline.
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- About 3M Pipeline Corrosion Protection and Rehabilitation
- Build a CI/CD pipeline for API Management
- Pipeline transport
- ABS Rules, Guides and Guidance Notes
- What are Piping & Instrumentation Diagrams
- HVAC Design for Ships and Offshore Structures
- EcoStruxure™ Pipeline Management
- Pipelines 4.0
- Pipelines in Canada
- The oil and gas pipeline system
About 3M Pipeline Corrosion Protection and RehabilitationVIDEO ON THE TOPIC: Offshore pipeline
The pipelines include dedicated pipelines for specific consumers but excludes offshore crude pipelines, onshore well flow, feeder and collector pipelines. These standards are intended to ensure uniform application of design principles and to guide in selection and application of materials and components, equipment and systems and uniform operation and maintenance of the petroleum and petroleum products pipelines system and shall primarily focus on safety aspects of the employees, public and facilities associated with petroleum and petroleum products pipelines.
The entity shall thereafter take approval from its Board or highest decision making body for non-conformities and mitigation measures. Approval of the Board or highest decision making body of entity along with the compliance report, mitigation measures and implementation schedule shall be submitted to the Board within six months from the date of notification of these regulations.
The entity shall have proper records of the same. Such test record shall have been valid for the current operation. Alternatively, if such a record is not available, the entity shall produce in service test record of the petroleum and petroleum products pipelines network having been tested as per ASME B The self certification shall be submitted to the Board with mitigation plan and implementation schedule;.
It shall be necessary to comply with all statutory rules, regulations and Acts in force as applicable and requisite approvals shall be obtained from the relevant competent authorities for the petroleum and petroleum products pipelines system. All materials and equipments shall be selected to ensure safety and suitability for the condition of use.
All necessary calculations shall be carried out to verify structural integrity and stability of the pipeline for the combined effect of pressure, temperature, bending, soil or pipe interaction, external loads and other environmental parameters as applicable, during all phases of work from installation to operation.
Such calculations shall include but not limited to the following:. In no case minimum temperature for carbon steel pipelines shall be less than - 29 Deg C. Design factors to be used in design formula shall be as per Table 1 given below.
Consideration shall be given to but not restricted to the effect of the following pre-operational loads:. The required capacity needed to be relieved through surge relief valve shall be determined by carrying out the surge analysis for above different scenarios under which a surge may occur in the pipeline.
Pipeline crossing water bodies, marshy areas, swamps and areas with high water table, etc. The specific gravity of the same under empty or installation conditions shall be minimum 1. All underground pipes and its components shall be protected against corrosion using suitable external anti-corrosion coating or painting and cathodic protection system. All above ground piping and its components shall be protected against corrosion by providing suitable anti-corrosion painting or coating.
Overhead power lines should not be allowed directly above station equipment or buildings. Buried piping inside the terminal area shall have a minimum cover of 1 m from top of pipe to finished ground or grade level. However, Category B and C installations having chain Link Fencing shall be required to carry out Risk Assessment at least once every year for review of categorization of installation in line with MHA guidelines or recommendations.
The fencing shall be suitably earthed distinctly at minimum two places and locked or attended for the protection of the property and the public. Emergency exit gate shall be away from main gate and always be available for use of personnel evacuation during emergency. Cross country pipeline system shall be equipped with following:. It should be preferably located in higher elevations. Valves shall be provided for isolating sections of station piping in order to:. Block valves with remote shut off provision from the control room shall be provided at the inlet downstream of Tee and outlet up stream of Tee of the pump or intermediate pigging or terminal or delivery station piping to isolate the pipeline from station facilities in case of emergency at station.
In addition, Block valves shall be considered as under:. Station by-pass system shall be provided to facilitate flow of liquid hydrocarbon in the pipeline bypassing the pumping facilities inside the station premises.
Check Valves shall be installed to provide automatic blockage of reverse flow in the piping system, within the station, wherever required. Check valves, when provided to minimize pipeline backflow at locations appropriate for the terrain features e.
Factors such as topography of the location, ease of operation and maintenance including requirements for section line fill shall be taken into consideration in deciding the location of the valves. However, in any case the distance between two consecutive sectionalizing valves shall not be more than 50 km.
All blow down piping shall have double valve segregation. The valves shall be as close as possible near the upstream and downstream bank of the river and public water supply reservoirs for isolation of these portions of the pipeline and these valves must be remote operated.
Overhead power lines shall not cross directly over the process area of the valve station facilities. For LPG installations, Sectionalizing or Block valves with remote shut off provision from the control room shall be provided at the boundary of station pipeline inlet and outlet locations to isolate the station facility. At locations where valve stations are combined with pump or repeater stations, the requirements of safe distance and statutory clearance, as applicable, shall be followed.
Sectionalizing valve on the piggable section of pipeline shall be full bore type to allow safe passage of pigs. Isolation of earthing of actuator to be done to avoid interference in C.
Pipeline sectionalizing valve may be electrically or pneumatically or hydraulically operated. Valves used in mainline shall be with butt weld ends. Valves used in buried portion shall be with butt weld joints only, except at the locations where hot tapping operation is to be carried out for which, buried flanged end valve may be provided.
However, pigging facilities for pipeline from or to jetty or type of petroleum and petroleum products handled may be provided on need basis. Threaded joints may be permitted in the above ground stations or above ground section of SV stations only if a welded isolation valve is provided before it. The number of threaded joints for station piping shall be to the extent minimum.
The threaded joints, after tightening, may be seal welded. The number of flanged joints for station piping for LPG shall be to the extent minimum. All tapping or opening shall be minimum 20 mm dia. Appropriate type of meters or other equivalent measuring device with the desired accuracy shall be installed at all pumping or terminal stations for leak detection or other purposes.
All electrical equipment operating above volts shall have two separate and distinct connections to earth grids. Separate earthing grid shall be provided for instrument and electrical system.
Self conducting structures having metal thickness of more than 4. They shall, however, be connected to the earthing system, at least, at two points at the base. SIS protects against the possibility of a process excursion developing into an incident and limits the excursion potential.
Emergency Shutdown ESD ii. Surge Relief iii. Alarm for hydrocarbon level in the tank iv. Hydrocarbon detectors vi. A reliable and dedicated communication system to interact between all stations including sectionalizing valve station with or without remote operation capability along the entire pipeline shall be designed and installed and maintained to ensure safe operations under both normal and emergency situations.
Online water analyzer may be installed at the originating pump station to detect any free water in the LPG being pumped. LPG Pumps shall be provided with a high point vent to safe height minimum 3 meters above the pump in case of no pump shed or 1. Wherever pumps are installed in series, shall have check valve in the header isolating the suction and discharge piping connection. The last pump in the series shall have check valve on the discharge piping. Additional common check valves shall be installed in the outlet header of the series pump configuration.
The suction and discharge side of the main pumps and booster pumps shall have actuated valves. Low suction pressure of booster and main pump. High discharge pressure at main pump. Low discharge pressure trip on pump against pipe rupture to avoid liquid vaporization. High Casing temperature e. High bearing temperature f.
Tripping of main or booster pump in case of closure of suction or discharge MOVs. Pump shall operate in sequence with defined logic at starting and shut down. Screwed pipe fittings shall not be used on any part of the fuel system piping or on the day service tank. Seamless tubing with stainless compression fittings are recommended. If the flame arrestor or traps are installed on the exhaust, it shall comply with BS In addition to this, provision shall be made for shut down of the engine on high coolant or lubricating oil temperature.
Depending upon requirement, pump station should have an instrument air supply system for instrumentation system, control valves etc. Electrical motor driven or engine driven air compressors shall be used. Air receivers, air storage bottles and instrument air dryer units shall be provided. The audio visual indication shall be provided at local panel and the pipeline control room.
Operation of the emergency shutdown system shall also shutdown all Pumps, Prime movers, Control valves and delivery manifold valves except those that are necessary for protection of the equipment.
The discharge of TRVs shall be connected to blow down drain connected to a sump tank of appropriate capacity. These TRVs shall have isolation valves on both sides of safety valve.
All TRV isolation valves upstream and downstream shall be lock open. In this case, isolation valves on downstream of PSVs are not required.
A weep hole with nipple at low point shall be provided on the vent pipe in order to drain the rain water which may get accumulated otherwise. Weep hole nipple shall be so oriented that in case of safety valve lifting and consequent fire resulting from LPG coming out from weep hole does not impinge on the structure or equipment.
A loose fitting rain cap with chain non sparking shall be fitted on top of the vent pipe. Discharge from safety valves shall be connected to a close blow down system having an underground storage tank of appropriate capacity. In case surge protection measures are installed, the sump tank shall have adequate capacity to store the excess liquid hydrocarbon expected to be released as result of activation of surge relief system.
The same may be coupled with suitable extinguishing system such as foam system for extinguishing the fire. Manual call point with talk back facilities shall be installed in the strategic locations of large size tank farm and to be hooked up with station fire alarm panel.
Low ductility materials such as cast iron, semisteel, malleable iron and cast aluminum shall not be used in any pipe. Insulation and weather proofing shall be fire retardant. Steel surfaces covered by insulation shall be properly coated to prevent corrosion. For sour liquid service requirements as per Schedule 1H shall be complied with.
Designed to accommodate future capacity expansion, the Pipestone Processing Facility will provide Encana with 19, barrels per day of net raw condensate processing capacity plus million cubic feet per day of net inlet natural gas processing capacity. We supplied three pipeline compressor trains driven by SGT gas turbines to a Mexican midstream operator, Fermaca, for the El Encino compression station pipeline project in Chihuahua. The trains recently became operational and play a key role in transporting natural gas from Waha, Texas, to power plants and industrial parks in Chihuahua, Coahuila and Durango, as well as to central and western Mexico. Our gas turbine models range from 4 to MW, fulfilling the requirements of a wide spectrum of applications in terms of efficiency, reliability, flexibility, and environmental compatibility.
Build a CI/CD pipeline for API Management
Learn More. Keyword Search:. All modern desktop printers are PostScript compatible. Some network printers are not. If you experience difficulty, please contact your IT department or download the necessary driver from the Adobe website. Download the Adobe PostScript Driver. Except for the permission granted below, nothing contained herein shall be construed as conferring upon the user in any manner any license, title or ownership of or in any intellectual property right of ABS.
United States. Interior and Insular Affairs. Sayfa Appendix IV. In a zone of the high seas contiguous to its territorial sea, the coastal State may exercise the control necessary to: a Prevent infringement of its customs, fiscal, immigration or sanitary regulations within its territory or territorial sea ; b Punish infringement of the above regulations committed within its territory or territorial sea. Sayfa - The Congress authorizes and directs that, to the fullest extent possible: 1 the policies, regulations, and public laws of the United States shall be interpreted and administered in accordance with the policies set forth in this Act Sayfa - State may take the necessary steps in its territorial sea to prevent passage which is not innocent.
The range of topics covered by the more than articles is Tam incelemeyi okuyun. Encyclopaedia of Occupational Health and Safety , 3. Poultry Processing Tory Ashdown 67 Forestry Peter Poschen Chapter Editor. Bleaching George Astrakianakis and Judith Anderson 72 8. Woodworking Jon Parish Chapter Editor. Prevention of Occupational Dermatosis among Workers Exposed.
ABS Rules, Guides and Guidance Notes
Signing up enhances your TCE experience with the ability to save items to your personal reading list, and access the interactive map. Pipelines are systems of connected pipes used to transport liquids and gases — namely oil and natural gas — across long distances from source to market. More than , km of pipelines criss-cross the country, part of a larger oil and gas sector that employs between , and , Canadians.
This website uses non-intrusive cookies to improve your user experience. You can visit our cookie privacy page for more information. Beta This is a new way of showing guidance - your feedback will help us improve it. Adopted 29 May ; came into force 29 November Additionally, there are details of how the different products are classified, the technical requirements that must be satisfied, and the conformity assessment procedures that must be followed. See FAQ section for advice on how to comply with the ESRs - essentially, by either producing a technical file that addresses each ESR in turn, or manufacturing using standards that have been listed in the EU's Official Journal which give a 'presumption of conformity' to specific ESRs. Annex C has an easy-to-use flow chart showing how equipment should be classified depending on, for example, what it is designed to contain and the operating pressure; also the conformity assessment procedure to be followed before placing the equipment on the market. Note: The Regulations do not apply to the assembly of pressure equipment on the site and under the responsibility of the user, as in the case of industrial installations. In such cases, the Pressure Systems Safety Regulations , which contain 'in use' provisions, will apply.
What are Piping & Instrumentation Diagrams
The pipelines include dedicated pipelines for specific consumers but excludes offshore crude pipelines, onshore well flow, feeder and collector pipelines. These standards are intended to ensure uniform application of design principles and to guide in selection and application of materials and components, equipment and systems and uniform operation and maintenance of the petroleum and petroleum products pipelines system and shall primarily focus on safety aspects of the employees, public and facilities associated with petroleum and petroleum products pipelines. The entity shall thereafter take approval from its Board or highest decision making body for non-conformities and mitigation measures. Approval of the Board or highest decision making body of entity along with the compliance report, mitigation measures and implementation schedule shall be submitted to the Board within six months from the date of notification of these regulations. The entity shall have proper records of the same.
HVAC Design for Ships and Offshore Structures
Oil and gas produced from a field need to be transported to customers. On many oil fields, oil is loaded directly on to tankers buoy-loading. In other cases, oil and gas are transported by pipeline to onshore facilities. Oil, wet gas and liquefied natural gas LNG are transferred to ships at onshore facilities, while dry gas is moved by pipeline to the UK and continental Europe. In contrast to the oil and gas fields on the Norwegian shelf, where the companies themselves are responsible for the operations, the gas pipeline system is more directly controlled by the authorities. An important consideration for the authorities is to ensure equal access to capacity in the system on the basis of companies' needs.
EcoStruxure™ Pipeline Management
Pipeline , line of pipe equipped with pumps and valves and other control devices for moving liquids, gases, and slurries fine particles suspended in liquid. Pipeline sizes vary from the 2-inch- 5-centimetre- diameter lines used in oil-well gathering systems to lines 30 feet 9 metres across in high-volume water and sewage networks.
Pipeline transport is the long-distance transportation of a liquid or gas through a system of pipes —a pipeline—typically to a market area for consumption. Liquids and gases are transported in pipelines and any chemically stable substance can be sent through a pipeline. Pipelines are useful for transporting water for drinking or irrigation over long distances when it needs to move over hills , or where canals or channels are poor choices due to considerations of evaporation , pollution , or environmental impact.
Pipelines in Canada
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The oil and gas pipeline system
APIs have become mundane. They have become the de facto standard for connecting apps, data, and services. In the larger picture, APIs are driving digital transformation in organizations. It allows organizations to automate deployment of API changes without error-prone manual steps, detect issues earlier, and ultimately deliver value to end users faster.