Engineering Standard SAES-A-400 Industrial Drainage Systems 26 October 2015 Document Responsibility: Industrial Drainage Standards Committee Saudi Aramco DeskTop Standards Table of Contents 1 Scope................................................................. 3 2 Conflicts and Deviations..................................... 4 3 References......................................................... 5 4 Definitions........................................................... 7 5 General Requirements....................................... 9 6 Drain Requirements for Specific Applications.. 13 7 Tank Dewatering.............................................. 15 8 Appendices....................................................... 15 Appendix I – Simplified Schematic of Industrial Drainage Systems........ 16 Previous Issue: 14 April 2014 Next Planned Update: 26 October 2018 Page 1 of 16 Primary contact: Qahtani, Salem M. (qahtansm) on 966-3-8801337 Copyright©Saudi Aramco 2015. All rights reserved. Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems SAES-A-400 Revision Log (exclude format or minor edit changes) # Section 1 1.4 Title Scope 2 3 References 3 5.5 General Requirements General Requirements 4 5.6 5 5.9 7 6 General Requirements General Requirements Table 8 6.10 Table 9 Appendix 1 Schematic 6 5.17 Change Removed reference to Sulfur Recovery Plants exclusion. Sulfur Recovery Plant CDS is licensor specific so the design is left as an open art for the sulfur recovery licensor based on evolving best industry practices Removed reference to and commentary note on SAES-A-402 because this standard does not exist at this time Removed OWDS system design conditions. The constraints for the design of lift station are in OWDS standard (SAES-S-020) Removed OWLS pump requirements because the requirements are already in OWDS standard. Also, removed mandate to install CDS which is in contradiction with cost and risk analysis per SAEP-125 Deleted because SAES-A-402 does not exist Added heel recovery requirement which was previously in SAES-A-401 Added “Toxic” with “Flammable” to emphasize that CDS also recovers toxic fluid Removed reference to Bulk Plant because a sump is acceptable. Updated Note 3 to state that Bulk Plants may use existing sump but Bulk Plants should use a segregated hydrocarbon piping network to avoid mixing flammable fluid in OWDS piping network. The constraints for sump design are in SAES-S-020 Replaced the schematic with a process flow diagram with symbology for P&IDs Page 2 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 1 SAES-A-400 Industrial Drainage Systems Scope 1.1 The purpose of this standard is to provide general guidelines for the selection of a proper drainage system to ensure that all liquids can be drained safely with minimum risk of fire or injury. Full conformance to this standard will ensure that facility drainage systems are capable of handling draining during both normal operations and during maintenance, and turnaround and inspections (T&I). Specifically, this standard provides general guidelines for design and safe handling of: 1.1.1 liquid hydrocarbons, 1.1.2 toxic liquids, 1.1.3 chemicals, 1.1.4 corrosive liquids, 1.1.5 aqueous materials, and 1.1.6 other liquid effluents that are drained in Saudi Aramco’s onsite and offsite facilities, including but not limited to transportation pipelines, tank farms and other types of hydrocarbons processing or handling facilities. 1.2 This standard covers all types of industrial liquid drains including, but not limited to, the following: 1.2.1 instrument bridles and sight glasses 1.2.2 thermal relief valves on liquid piping 1.2.3 pump and compressor casings 1.2.4 knockout drums 1.2.5 process vessels and separators 1.2.6 heat exchangers 1.2.7 filters 1.2.8 reactors 1.2.9 fractionation columns 1.2.10 scraper launchers / receivers Page 3 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems 1.2.11 bulk plants loading, unloading and heel recovery 1.2.12 loading arms 1.2.13 low pressure and atmospheric product storage tanks 1.2.14 hydrocarbon storage tanks’ dewatering systems 1.2.15 sample points 1.2.16 low point drains from control valves and piping systems 1.3 2 This standard does not cover: 1.3.1 The environmental design aspects of treating collected liquids from industrial drainage and oily water drainage systems (refer to SAES-A-103 and SAES-A-104). 1.3.2 The drain systems of laboratories or dedicated battery rooms (SAES-P-103) governed by SAES-S-060. 1.3.3 The offshore platform drainage systems (SAES-A-403). 1.4 For retroactive applications of this standard to existing facilities, refer to SAEP-125, Paragraph 3.1. 1.5 For conceptual understanding of relationships between oily water and closed drain systems, refer to simplified schematics under Appendix I for Process Areas. THE SCHEMATICS NEITHER SUPERSEDE THE REQUIREMENTS OF THIS STANDARD NOR DO THEY DICTATE THE CONFIGURATION OF A CLOSED DRAIN SYSTEM OR AN OILY WATER DRAINAGE SYSTEM. Conflicts and Deviations 2.1 Any conflicts between this Standard and other applicable Saudi Aramco Engineering Standards (SAESs), Saudi Aramco Materials System Specifications (SAMSSs), Saudi Aramco Standard Drawings (SASDs), or industry standards, codes, and forms shall be resolved in writing by the Company or Buyer Representative through the Manager, Process & Control Systems Department of Saudi Aramco, Dhahran. 2.2 Direct all requests to deviate from the Standard in writing to the Company or Buyer Representative, who shall follow internal company procedure SAEP-302 and forward such requests to the Manager, Process & Control Systems Department of Saudi Aramco, Dhahran. Page 4 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 3 SAES-A-400 Industrial Drainage Systems References All referenced Specifications, Standards, Codes, Forms, Drawings, and similar material shall be considered part of this Standard to the extent specified herein and shall be the latest issue (including all revisions, addenda, and supplements) unless stated otherwise. 3.1 Saudi Aramco References Saudi Aramco General Instructions GI-0150.100 Hazardous Materials Communication (HAZCOM) Program GI-0430.001 Implementing the Saudi Aramco Hazardous Waste Code Saudi Aramco Engineering Procedure SAEP-125 Preparation of Saudi Aramco Engineering Standards SAEP-302 Instruction for Obtaining a Waiver of a Mandatory Saudi Aramco Engineering Requirement SAEP-327 Disposal of Wastewater from Cleaning, Flushing and Dewatering Pipelines and Vessels Saudi Aramco Engineering Standards SAES-A-007 Hydrostatic Testing Fluids and Lay-Up Procedures SAES-A-103 Discharges to the Marine Environment SAES-A-104 Wastewater Treatment, Reuse and Disposal SAES-A-401 Closed Drain Systems SAES-A-403 Offshore Platform Drainage Systems SAES-B-005 Spacing and Diking for Atmospheric and LowPressure Tanks SAES-B-054 Access, Egress, and Materials Handling for Plant Facilities SAES-B-055 Plant Layout SAES-B-068 Electrical Area Classification SAES-B-070 Fire and Safety Requirements for Bulk Plants, Air Fueling and Sulfur Loading Facilities SAES-F-007 System Design Criteria for Flares Page 5 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems SAES-G-005 Centrifugal Pumps SAES-J-003 Instrumentation - Basic Design Criteria SAES-P-103 UPS and DC Systems SAES-S-010 Sanitary Sewers SAES-S-020 Oily Water Drainage Systems SAES-S-030 Storm Water Drainage Systems SAES-S-060 Saudi Aramco Plumbing Code Saudi Aramco Material Systems Specifications 16-SAMSS-503 Indoor Control Gear - Low Voltage 16-SAMSS-514 Control and Protective Relay Panel - Indoor Saudi Aramco Engineering Reports 3.2 SAER-5437 Guidelines for Conducting HAZOP Studies SAER-6168 Engineering Review Report for Oily Water Lift Stations Industry Codes and Standards American Society for Testing and Materials ASTM D97 Standard Test Method for Pour Point of Petroleum Products National Fire Protection Association NFPA 704 3.3 Identification of the Hazards of Materials for Emergency Response Saudi Government Documents and Standards The Saudi Government General Environmental Regulations, General Environmental Regulations 3.4 Chemical Hazard Bulletins (CHB’S) CHB# 14 Sodium Hydroxide (Caustic Soda) CHB# 47 Benzene CHB# 71 Phenol (Carbolic Acid) CHB# 155 Hydrogen Sulfide (H2S) CHB# 400 Sulfuric Acid Page 6 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 4 SAES-A-400 Industrial Drainage Systems CHB# 518 STADIS 450 (Anti-Static Additive) CHB# 666 Hot Pot – 922 (Corrosion Inhibitor) Definitions Chemical Hazard Bulletin (CHB): An internal company document (Available in both English & Arabic) developed by Environmental Protection Department to provide standardized one-page summary of a material’s hazard ratings that will specify health hazard, fire & reactivity, handling, storage & disposal and first aid information for use in the handling of hazardous materials. Use of CHBs shall be consistent with the requirements contained within GI-0150.100, Hazardous Materials Communication Program (HAZCOM) to ensure employees are knowledgeable of the hazards associated with the specific chemicals. Closed Drain System (CDS): A closed drain system is a piping collection system connecting selected hydrocarbon drains and is provided with recovery or safe disposal of collected liquids. A CDS is isolated from air or oxygen sources. (Refer to SAES-A-401). Combustible Liquid: A liquid that has a flash point greater than 54°C (130°F). Examples of such fluids are: diesel, transformer oils, C7+ feed stocks, bunker fuel, and sulfur (refer to SAES-B-005). Dewatering Effluent: Contaminated liquid water separated from a hydrocarbon storage tank that requires further treatment to separate and recover contained hydrocarbons away from water before water can be disposed off through a waste water treatment system in accordance with SAES-A-104. Flammable Liquid: A liquid that has a flash point equal to or less than 54°C (130°F). Examples of such fluids are: stabilized crude, gasoline, Jet A-1, Jet JP-4, Jet JP-8, C6 and lighter feed and blending stocks, and methanol. For purposes of this standard, a combustible liquid stored or processed at a temperature equal to or higher than 8°C (15°F) below its flashpoint shall be considered to be a flammable liquid (refer to SAES-B-005). Flash Point: The flash point of a flammable liquid is the lowest temperature at which it can form an ignitable mixture in air. At this temperature the vapor may cease to burn when the source of ignition is removed (refer to SAES-B-005). Flushing Oil: A lighter (greater API gravity) hydrocarbon liquid that is completely miscible and can be used to improve the fluidity of a high pour point hydrocarbon liquid. Health Hazard Materials: Any material or chemical for which there is statistically significant evidence based on at least one study conducted in accordance with established scientific principles that acute or chronic health effects may occur in exposed employees (as defined in GI-0150.100). Page 7 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems High Health Hazard Materials: High Health Hazard Materials, as defined herein, include: (a) (b) Materials with a Health Hazard rating of 3 or 4 per the Saudi Aramco Chemical Hazards Bulletins (CHBs), or per NFPA 704. Examples of such materials include but are not limited to: sodium hydroxide (caustic soda) – CHB# 14 benzene – CHB# 47 phenol (carbolic acid) – CHB# 71 hydrogen sulfide (H2S) – CHB# 155 sulfuric acid – CHB# 400 STADIS 450 – (anti-static additive) – CHB# 518 hot pot -922 (corrosion inhibitor) – CHB# 666 Highly corrosive materials such as acid, caustic and other materials injurious to personnel. Highly Corrosive Materials: For purposes of applying this Standard, aqueous materials with a pH level 1-3 (acid) or pH level 12-14 (base) which, on brief exposure, could cause major injury or destructive damage. High-Pour Point Materials: Materials that have a pour point within 10°C (18°F) of the ambient temperature. Influent Sump: A lift station installed at the inlet to an oily water separator. Inventory: All liquid contained in the vessel including contents in the piping to the nearest emergency shut down or block valve. Lift Station: A facility to pump effluent from a sump to a point of higher elevation (refer to SAES-S-020). Neutralization: For pH control, the Government allowable discharge is between 6 and 9 standard pH units. Discharge liquids must meet Government and SAES-A-104 definition of pH quality. Oily Water: Mixtures of hydrocarbon residues and water. Oily water is considered to be contaminated water released during normal operation. Note: Due to unforeseen conditions and during uncontrollable accidental situations such as during fire or spill-containment, the oily water drainage system may receive oilcontaminated wastewater with flammable hydrocarbons (refer to SAES-S-020). Page 8 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems Oily Water Drainage System (OWDS): A system that removes surface runoffs and effluents from process areas within a plot limit to a treatment facility, or off-plot pond area. It operates either by gravity or pumping force. The OWDS consists of catch basins, manholes, and a network of drainage piping consisting of sub-laterals, laterals, sub-mains and mains (refer to SAES-S-020 and SAER-6168). Pour Point: Pour point of a liquid is the lowest temperature at which the liquid will just flow under standards test conditions as defined by ASTM D97 [ASTM Standards Test Method for Pour Point of Petroleum Oils (D97/IP 15)]. Pressurized Hydrocarbons: Pressurized hydrocarbons shall mean that the pressure in the source equipment at the time of drainage is sufficient to overcome the hydraulic and static system pressure drop to transfer liquid hydrocarbons to a CDS. Process Areas: All physical areas of a facility that involve processing, handling and treating of hydrocarbons including any sources of ignition. Typical outside process area facilities include tank farms, pipelines, waste water ponds, etc. Tank Dewatering System: A system to remove settled water from atmospheric hydrocarbon storage tanks. (For flammable liquid tanks refer to SAES-A-401, and for combustible liquid tanks refer to SAES-S-020.) Toxic: Any material with health hazard 3 or 4 as defined by NFPA 704. 5 General Requirements Selection of the type of drainage system shall be based on the following design and operating philosophy: 5.1 Combustible, flammable, high health hazard, toxic, corrosive, or high-pour point liquid materials shall not be drained into the oily water drainage system (OWDS) (SAES-S-020), storm water drainage system (SAES-S-030), or sanitary sewer system (SAES-S-010) except as provided for under Section 6 of this standard. 5.2 Any facility handling flammable and combustible liquid hydrocarbons, toxic or high health hazard materials shall have a closed drain system (CDS) designed in accordance with SAES-A-401. This requirement is applicable to new or existing facilities. Existing facilities may use available systems to meet the intent of CDS definition under Section 4. 5.3 All flammable and combustible liquid hydrocarbons, toxic and high health hazard materials shall be drained to CDS. Page 9 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 5.4 SAES-A-400 Industrial Drainage Systems No pressurized flammable and combustible liquid hydrocarbons and high health hazard materials shall be drained to an OWDS. In order to minimize drainage to CDS, product or intermediate process streams shall be diverted to an off-specification system (e.g., during startup, emergency or shutdown of downstream equipment). After draining of equipment inventory into CDS, residual inventories of flammable and combustible liquids and high health hazard materials shall be flushed with water for a minimum of three volume flushes (water shall not react with material). After the flush less than 0.1 m³ (26 US gallons) from equipment may be drained to the OWDS. 5.4.1 If draining to the OWDS, the sewer shall be flushed with water for further dilution after draining such flammable and combustible liquids and high health hazard materials. Water flushing in the equipment shall continue until percent lower explosive limit (%LEL) determined by manual test, by lowering the %LEL tester sample hose near the liquid indicates <10% of the LEL tester indication and H2S content less than 10 ppm. Operational Commentary: Prior to flushing with water in the equipment, reduce inventory to minimum, preferably <0.1 m³ (26 US gallons) to conserve water. 5.4.2 Draining flammable and combustible liquids and high health hazard materials to OWDS under above guideline is subject to: (a) wind direction, (b) positioning of any ignition source beyond 15 m, (c) H2S content less 10 ppm, and (d) use of proper safety personal protective equipment (PPE) including breathing apparatus. Operational Commentaries: 5.5 (1) Contact Environmental Compliance Division for recommendation of PPE, which will include skin, eye, and respiratory protection for the relevant chemical hazard. (2) Foreman and/or Shift Superintendent responsible for the operation of oily wastewater treatment system shall be informed prior to the draining of these hydrocarbon liquids. This is required in order to prevent failure of the treatment system and the violation of environmental regulations. For T&I or equipment maintenance, the system shall be designed to drain and depressurize equipment to CDS. Provision for N2 or fuel gas to transfer any residual, low pressure flammable and combustible liquids and high health hazard materials to CDS shall be provided, except for existing equipment where design pressures do not allow pressurization by N2 or fuel gas. Depressurized Page 10 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems equipment drains (normally closed and blinded) may be opened to OWDS only to confirm that all flammable and combustible liquids and high health hazard materials have been completely drained. Operational Commentary: Since the CDS system is heavily utilized during plant/unit T&I, it is probably best to schedule the T&I of the CDS while the operating unit is in service. The Operations & Maintenance Manual shall provide for temporary arrangements and precautions for any emergency drainage through the OWDS while the CDS in undergoing its T&I. 5.6 The design of OWDS shall be in accordance with SAES-S-020. The lift station pump(s) requirements shall be in accordance with SAES-G-005 and designed to safely operate under the requirements of SAES-B-068. In addition, a power monitor shall be provided to trip lift station pumps on loss of flow. All motors on lift station pumps shall include an under power trip function implemented in the control gear protection relay, as per 16-SAMSS-503 and 16-SAMSS-514. The under power feature shall be set and tested such that it will trip the pump only on dry-run and no-flow conditions and shall not cause nuisance trips. The under power trip is in “addition-to” other required low-flow trips on lift station pumps as specified by SAES-S-020. 5.7 High pour point materials, like asphalt, demex pitch, etc., shall be drained to a dedicated concrete pit that is designed for high temperature service and shall maintain the temperature of the drained material at least 10°C (18°F) above the pour point. 5.7.1 Draining high pour point liquids in OWDS is prohibited since this could cause plugging. 5.7.2 High-pour point materials that can be safely mixed with flushing oils or diesel to improve fluidity shall be drained to CDS. 5.7.3 Accumulated liquids may be disposed by a vacuum truck. 5.8 No liquids drainage piping of any kind shall be directly connected into the gas flare system. 5.9 All sour water separated from hydrocarbon processing equipment shall be directed to sour water treatment facilities. Hydrocarbon contaminated water shall be handled in accordance with SAES-A-401. 5.10 All equipment drain piping to an OWDS shall be isolated by double isolation (e.g., one block and bleed valves with plug or blind flange). Page 11 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems Commentary: To assure drain piping tightness and avoid potential piping dead leg, one block valve shall be installed at or close to equipment outlet nozzle or at drain piping take off and the second isolation shall be located near OWDS funnel. Blind or plug shall be installed downstream the second block valve. 5.11 All liquid drain systems shall be designed and conformed to the formal Hazard and Operability (HAZOP) methodology following the guidelines in HAZOP Engineering Report SAER-5437. 5.12 Hot steam condensate shall be directed to the condensate recovery system. Operational Commentaries: 1. In the event of any contamination of steam condensate with hydrocarbons, identify the source of contamination and isolate for correction. 2. If for any reason, hydrocarbon-contaminated hot steam condensate is directed to OWDS, then it must be cooled by dilution with utility or fire water before entering OWDS. 5.13 For the design of OWDS and CDS for an offshore facility refer to SAES-A-403. 5.14 The disposal of wastewater from cleaning, flushing and dewatering pipelines, tanks, and vessels at onshore facilities shall be in accordance with SAEP-327. Hydrostatic test waters shall be disposed off in accordance with the requirements of SAEP-327 and SAES-A-103; and disposal plans must be approved prior to the start of any hydrotest in accordance with SAES-A-007. 5.15 For continuous liquid drainage flow, the size of the drainage pipe shall not be reduced in size in the direction of the flow. 5.16 Plants for loading/unloading of products from trucks shall be provided with heel recovery to empty such products from the trucks when necessary into collection facilities. Operations will also ensure heels recovered or transferred from such truck tanks are properly analyzed to ensure compatibility of contents to avoid inadvertent chemical or exothermic/endothermic reactions. Commentary: Heel recovery facilities are intended to end practices that discharge truck contents to the environment prior to loading products. Such practices have the potential of soil/ground water contamination, toxic/flammable vapors and in general impact on health, safety and environment. Provision of heel recovery facility will prevent such practices and ensure alignment with the national directive. Page 12 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 6 SAES-A-400 Industrial Drainage Systems Drain Requirements for Specific Applications Drain system design for specific flammable and combustible liquids drain applications shall be as follows: Flammable/Toxic Liquids Combustible Liquids CDS1 CDS1 (except as provided under 5.4) CDS or route to storage or holding vessel OWDS or route to storage or holding vessel Drain Points3 6.1 Instrument Bridles and Sight Glasses 6.2 Thermal Relief Valves on Liquid Piping 6.3 Pump and Compressor Casings CDS CDS (except as provided under 5.4) 6.4 Knockout Drums CDS CDS (except as provided under 5.4) 6.5 Process Vessels and Separators CDS CDS (except as provided under 5.4) 6.6 Heat Exchangers CDS CDS (except as provided under 5.4) 6.7 Filters CDS CDS (except as provided under 5.4) 6.8 Reactors CDS CDS (except as provided under 5.4) 6.9 Scraper Launchers/Receivers CDS2 CDS2 (except as provided under 5.4) CDS CDS (except as provided under 5.4) Refer to Section 7.1 of this standard Refer to Section 7.2 of this standard 6.12 Sample Points Flush CDS CDS (except as provided under 5.4) Low Point Drains from Control 6.13 Valves, Custody Metering Stations and Piping Systems CDS1 CDS1 (except as provided under 5.4) 6.10 Ship Loading Arms 6.11 Hydrocarbon Storage Tanks’ Dewatering Systems Notes: 1. Temporary drain connections as allowed by Section 6.5.5.6 of SAES-A-401 may be used. 2. Exception for Scraper Launchers/Receivers: Page 13 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems In remote locations, where a CDS is neither justified nor practicable, a collection vessel without a pump shall be provided. The design shall include but not limited to the following: a) A detailed drawing showing the arrangement for the Scraper Launchers/Receivers drainage system and the collection vessel construction. The collection vessel volume shall be properly sized to handle the maximum flow rate to meet the design drain basis of the scraper launchers/receiver. b) Drain shall be hard piped to the collection vessel and the hard-pipe drain network shall be sized for closed drainage system utilizing gravity drainage. c) The collection vessel shall be fitted with a pump out pipe with quick connector, dust cap and chain design to allow tankers to vacuum out the content of the collection vessel for disposal in accordance with GI-0430.001. d) The collection vessel shall be fitted with a 4-inch vent extending 3 meters above ground and at a location 15 meters minimum downwind from any ignition source as per SAES-S-020. For collection vessels receiving sour hydrocarbons, the vent height and minimum location downwind from personnel or any ignition source shall not be less than the requirements of SAES-S-020 and shall be concurred in writing with the Loss Prevention Department and the Chairman, Industrial Drainage Standards Committee. e) The collection vessel shall have a level instrument with local siren alarm in accordance with SAES-J-003. f) For collection of scraper/receiver drains, collection vessel shall be installed below grade in accordance with requirements of SAES-D-116. g) Hydrocarbons from scraper launcher and receivers shall not be drained to an OWDS or grade. 3. For Bulk Plants, Flammable Hydrocarbon may drain into the same sump that receive oily water drains from the plant. However, a dedicate hydrocarbon drain network shall be used to avoid mixing hydrocarbon with Oily Water Drain piping network. 7 Tank Dewatering All hydrocarbon tanks that require dewatering shall be equipped for water drainage. 7.1 Dewatering effluent from flammable hydrocarbon storage tanks shall be in accordance with SAES-A-401. 7.2 Dewatering effluent from combustible hydrocarbon storage tanks may be drained to OWDS in accordance with SAES-S-020. Commentary: High pour point materials from storage tanks shall not be drained to OWDS. These streams shall be drained in accordance with paragraph 5.8. Page 14 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 8 SAES-A-400 Industrial Drainage Systems Appendices For conceptual understanding of relationships between OWDS and CDS, refer to simplified schematics as follows: Appendix I - Process Areas The schematic DO NOT SUPERSEDE requirements of this standard. 26 October 2015 Revision Summary Major revision to align the document with industry standards, guidelines and best practices. Page 15 of 16 Document Responsibility: Industrial Drainage Standards Committee Issue Date: 26 October 2015 Next Planned Update: 26 October 2018 SAES-A-400 Industrial Drainage Systems Appendix I - Simplified Schematic of Industrial Drainage Systems (This schematic DOES NOT SUPERSEDE requirements of this standard.) Page 16 of 16