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API PUBL 421 - MONOGRAPHS ON REFINERY ENVIRONMENTAL CONTROL - MANAGEMENT OF WATER DISCHARGES DESIGN AND OPERATION OF OIL-WATER SEPARATORS - FIRST EDITION; ERRATA 9/1992 Organization: API
Date: 1990-02-01
Description: The purpose of this monograph is to provide design guid- ance on gravity-type oil-water separators for use in petro- leum refineries, to provide practical advice on solving operating problems and improving separator performance, and to present information on the performance of existing separators.
COE ETL 1110-3-466 - SELECTION AND DESIGN OF OIL/WATER SEPARATORS AT ARMY FACILITIES Organization: COE
Date: 1994-08-26
API SPEC 12J - SPECIFICATION FOR OIL AND GAS SEPARATORS - EIGHTH EDITION Organization: API
Date: 2008-10-01
Description: General This specification covers minimum requirements for the design, fabrication, and shop testing of oil-field type oil and gas separators and/or oil-gas-water separators used in the production of oil and/or gas, and usually located but not limited to some point on the producing flowline between the wellhead and pipeline.
API STD 12J - SPECIFICATION FOR OIL AND GAS SEPARATORS - THIRD EDITION Organization: API
Date: 1962-03-01
Description: This specification covers minimum requirements for the design fabrication and plant testing of oilfield type oil and gas separators and/or oil-gas-water separators used in the production of oil and/or gas, and usually located at some point on the producing flow line between the wellhead and pipeline.
CSA Z662 - OIL AND GAS PIPELINE SYSTEMS - SEVENTH EDITION; INCORPORATES ERRATA: MARCH 2016 AND ERRATA: JULY 2016 Organization: CSA
Date: 2015-01-01
Description: This Standard does not apply to a) piping with metal temperatures below –70 °C; b) gas piping beyond the outlet of the customer’s meter set assembly (covered by CSA B149.1); c) piping in natural gas liquids extraction plants, gas processing plants (except main gas stream piping in dehydration and all other processing plants installed as part of gas pipeline systems), gas manufacturing plants, industrial plants, and mines; d) oil refineries, terminals other than pipeline terminals, and marketing bulk plants; e) abandoned piping; f) in-plant piping for drinking, make-up, or boiler feed water; g) casing, tubing, or pipe in oil or gas wells, wellheads, separators, production tanks, and other production facilities; h) vent piping for waste gases of any kind operating at or near atmospheric pressure; i) heat exchangers; j) liquefied natural gas systems (covered by CSA Z276); k) liquid fuel distribution systems; l) loading/unloading facilities for tankers or barges; m) refuelling facilities; and n) hydrocarbon storage in underground formations and associated equipment (covered by CSA Z341 Series).
ASTM F2283 - STANDARD SPECIFICATION FOR SHIPBOARD OIL POLLUTION ABATEMENT SYSTEM Organization: ASTM
Date: 2012-06-01
Description: OPAS is comprised of drain tanks, bilge suctions, transfer pumps, Oily Bilge Water Holding Tanks, Oil Residue (sludge) Tanks, 15 ppm Bilge Separator systems, 15 ppm Bilge Alarm, automatic stopping device, and deck connections.
NBN - EN 858-1/A1 - SEPARATOR SYSTEMS FOR LIGHT LIQUIDS (E.G. OIL AND PETROL) - PART 1: PRINCIPLES OF PRODUCT DESIGN, PERFORMANCE AND TESTING, MARKING AND QUALITY CONTROL Organization: NBN
Date: 2005-01-01
Description: This standard deals with installations for the separation of light liquids (e.g. oil and petrol), i.e. those with a density up to 0.95 g/cm3 from waste water by means of gravity and/or coalescence.
NBN - EN 858-1 - SEPARATOR SYSTEMS FOR LIGHT LIQUIDS (E.G. OIL AND PETROL) - PART 1: PRINCIPLES OF PRODUCT DESIGN, PERFORMANCE AND TESTING, MARKING AND QUALITY CONTROL Organization: NBN
Date: 2002-03-08
Description: This standard deals with installations for the separation of light liquides (e.g. oil and petrol), i.e. those with a density up to 0.95 g/cm3 from waste water by means of gravity and/or coalescence.
NBN - EN 858-1/A1 - SEPARATOR SYSTEMS FOR LIGHT LIQUIDS (E.G. OIL AND PETROL) - PART 1: PRINCIPLES OF PRODUCT DESIGN, PERFORMANCE AND TESTING, MARKING AND QUALITY CONTROL Organization: NBN
Date: 2005-01-01
Description: This standard deals with installations for the separation of light liquids (e.g. oil and petrol), i.e. those with a density up to 0.95 g/cm3 from waste water by means of gravity and/or coalescence.
NBN - EN 858-1 - SEPARATOR SYSTEMS FOR LIGHT LIQUIDS (E.G. OIL AND PETROL) - PART 1: PRINCIPLES OF PRODUCT DESIGN, PERFORMANCE AND TESTING, MARKING AND QUALITY CONTROL Organization: NBN
Date: 2002-03-08
Description: This standard deals with installations for the separation of light liquides (e.g. oil and petrol), i.e. those with a density up to 0.95 g/cm3 from waste water by means of gravity and/or coalescence.
ASTM C913 - STANDARD SPECIFICATION FOR PRECAST CONCRETE WATER AND WASTEWATER STRUCTURES Organization: ASTM
Date: 2016-07-01
Description: NOTE 1—Water and wastewater structures are defined as solar heating reservoirs, cisterns, holding tanks, leaching tanks, extended aeration tanks, wet wells, pumping stations, distribution boxes, oil-water separators, treatment plants, manure pits, catch basins, drop inlets, and similar structures.
VA 23 23 00 - REFRIGERANT PIPING Organization: VA
Date: 2010-02-01
Description: The schematic piping diagram shall show all accessories such as, stop valves, level indicators, liquid receivers, oil separator, gauges, thermostatic expansion valves, solenoid valves, moisture separators and driers to make a complete installation.
API SPEC 12L - SPECIFICATION FOR VERTICAL AND HORIZONTAL EMULSION TREATERS - FIFTH EDITION;EFFECTIVE DATE: APRIL 1, 2009 Organization: API
Date: 2008-10-01
Description: The function of the treater is to dehydrate (or dewater) the produced crude oil to a specified level of basic sediment and water (BS&W). Oil-water separation may be enhanced by heating, emulsion breaking chemicals, coalescing media, and/or electrostatic fields in vessels sized for substantial liquid residence time.
DS/EN 12693 - REFRIGERATING SYSTEMS AND HEAT PUMPS - SAFETY AND ENVIRONMENTAL REQUIREMENTS - POSITIVE DISPLACEMENT REFRIGERANT COMPRESSORS Organization: DS
Date: 2008-06-13
Description: For semi-hermetic and open drive compressors which include moving parts and for which the external envelope is primarily designed for mechanical loads, thermal loads (to limit the possible deformation due to temperature), stiffness of the structure (external mechanical loads and weight of the equipment), taking into account established safe industrial practice, it is considered that pressure is not a significant design factor.Attached parts covering other functions e.g. oil separators, oil coolers, suction accumulators shall comply to EN 14276-1 or EN 13445-6 (cast iron) or prEN 13445-8:2003 (aluminium) or showing compliance to the relevant European requirements.
NBN - EN 12693 - SYSTÈMES DE RÉFRIGÉRATION ET POMPES À CHALEUR - EXIGENCES DE SÉCURITÉ ET D'ENVIRONNEMENT - COMPRESSEURS VOLUMÉTRIQUES POUR FLUIDES FRIGORIGÈNES Organization: NBN
Date: 2008-11-01
Description: For semi-hermetic and open drive compressors which include moving parts and for which the external envelope is primarily designed for mechanical loads, thermal loads (to limit the possible deformation due to temperature), stiffness of the structure (external mechanical loads and weight of the equipment), taking into account established safe industrial practice, it is considered that pressure is not a significant design factor.Attached parts covering other functions e.g. oil separators, oil coolers, suction accumulators shall comply to EN 14276-1 or EN 13445-6 (cast iron) or prEN 13445-8:2003 (aluminium) or showing compliance to the relevant European requirements.
NBN - EN 12693 - REFRIGERATING SYSTEMS AND HEAT PUMPS - SAFETY AND ENVIRONMENTAL REQUIREMENTS - POSITIVE DISPLACEMENT REFRIGERANT COMPRESSORS Organization: NBN
Date: 2008-11-01
Description: For semi-hermetic and open drive compressors which include moving parts and for which the external envelope is primarily designed for mechanical loads, thermal loads (to limit the possible deformation due to temperature), stiffness of the structure (external mechanical loads and weight of the equipment), taking into account established safe industrial practice, it is considered that pressure is not a significant design factor.Attached parts covering other functions e.g. oil separators, oil coolers, suction accumulators shall comply to EN 14276-1 or EN 13445-6 (cast iron) or prEN 13445-8:2003 (aluminium) or showing compliance to the relevant European requirements.
NBN - EN 12693 - REFRIGERATING SYSTEMS AND HEAT PUMPS - SAFETY AND ENVIRONMENTAL REQUIREMENTS - POSITIVE DISPLACEMENT REFRIGERANT COMPRESSORS Organization: NBN
Date: 2008-11-01
Description: For semi-hermetic and open drive compressors which include moving parts and for which the external envelope is primarily designed for mechanical loads, thermal loads (to limit the possible deformation due to temperature), stiffness of the structure (external mechanical loads and weight of the equipment), taking into account established safe industrial practice, it is considered that pressure is not a significant design factor.Attached parts covering other functions e.g. oil separators, oil coolers, suction accumulators shall comply to EN 14276-1 or EN 13445-6 (cast iron) or prEN 13445-8:2003 (aluminium) or showing compliance to the relevant European requirements.
IEC 62282-3-1 - FUEL CELL TECHNOLOGIES – PART 3-1: STATIONARY FUEL CELL POWER SYSTEMS – SAFETY - EDITION 1.0 Organization: IEC
Date: 2007-04-01
Description: – Fuel cell stack: Assembly of cells, separators, cooling plates, manifolds and a supporting structure that electrochemically coverts, typically, hydrogen rich gas and air reactants to d.c. power, heat, water and other byproducts.
CPC - CEMENT MANUFACTURER'S HAN - CEMENT MANUFACTURER'S HANDBOOK Organization: CPC
Date: 1979-04-07
Description: GRINDING MILL INVESTIGATION (ENGLISH SYSTEM OF UNITS) 18.01 Mill Critical Speed 18.02 Percent of Critical Speed 18.03 Ratio: Free Height to Mill Diameter 18.04 Internal Volume of Mill 18.05 Percent Loading of the Mill 18.06 Bulk Volume of Ball Charge 18.07 Weight of Ball Charge 18.08 Weight of Feed in Mill 18.09 Steel to Clinker Ratio 18.10 Bond's Laboratory Work Index 18.11 Power Required 18.12 Mill Power 18.13 True Specific Power Demand of Grinding Mill 18.14 Mill Operating Efficiency 18.15 Specific Surface Grinding Efficiency 18.16 Mill Size Ratio 18.17 Specific Mill Volume per Horsepower 18.18 Separator Load 18.19 Separator Efficiency 18.20 Circulating Load 18.21 Size of Grinding Balls Required Chapter 19.

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