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HomeMy WebLinkAboutGAS TANK PAPERWORKM1N.-i}P4Y•✓Y•Y✓•'�1r`FM�M•YT�+!L.�R'WM.�Xi� fv� SAC.Mj'P/Tq'iTY.V•'tl'^^iKf-.f•"di•�', 8" dome in black plastic or white galvanized steel ►`1IFI l�,l'F WhJ IMI IHIM�II POWDt7RA°}©heGureThtSupe"r©urableTopcua .+ with Zinc RIch'Pruner on Abouegrountl POWgURA�OneCure�'Twocoatsysfem!properhesincliide • '� • Zinc [ich:epoxpprimer;' • Super -durable TGIC; polyester,'#opcoat '1 •-Superior codosiomand.edgbprotectioq `'•. „ � Tatentpi hdllno formulated prunerand topcoat • Dual service options for above or underground applications • Option #1: Ready -to -bury red oxide durable powder coating with black • polyethylene AGUG dome' • Option #2: Aboveground option with steel 8" AGUG dome • All valves and float gauges are centered under dome • Fabricated to the latest A.S.M.E. Code, Section Vill, Division 1 • Registered with the National Board • #72liquid level outage valveorifice reduces refueling emissions • Vacuum pre -purged to save time, money and product 'Applicable federal, state, or local regulations may contain specific requirements for protective coatings and cathodic protection. The purchaser and installer are responsible for compliance with all federal, state, local and NFPA industry regulations. cathodic protection is required and coating must be continuous and uninterrupted and must comply with an local, state or national code. www.TrinityContainers.com Call Toll Free: 888-558-8265 TRINITI ®® o Containing Our World'; Energy - General Specifications Conforms to the latest edition of the ASME code for Pressure Vessels, Section Vill, Division 1. Complies with NFPA 58. Rated at 250 psig from -200 F. to 1250 F. All tanks may be evacuated to a full (14.7 psi) vacuum. Vessel Finish: Coated with epoxy red powder. ( Tanks coated with the epoxy powder must be buried). For Aboveground use, tanks may be coated with TGIC powder. Applicable federal, state or local regulations may contain specific requirements for protective coatings and cathodic protection. The purchaser and installer are responsible for compliance with all federal, state or local regulations. .�---�, WITHDRAWAL VALVE FLOAT �� � r.��Es`\ �` ANODE GAUGE] ®X CONNECTION FILLER I O VALVE \ n n / SERVICE/ MULnvALVE RELIEF VALVE FITTINGS LAYOUT UNDER DOME Rev. Jan. 27.2010 Why;Tanks Corrode Underground steel tanks corrode due to an electrochemical reaction between the tank and the surrounding soil. The process of corrosion occurs due to small voltage differences on the steel surface that result In the flow of DC current from ons location to another. Where current flows from the tank into the soil corrosion occurs. This location is called the anode Ina corrosion circuit. Where current flows from the soil to the tank, no corrosion occurs. The progress of corrosion is determined by the amount of current flowing between the anode and the cathode and whetherthe locations of the anode/ cathode remain constant overtime. Corrosion rates are generally higher in wet soil environments since the conductivity of the soil promotes the flow of DC current In the corrosion circuit. Corrosion generally exhibits Itself on underground tanks in either a general overall rusting or more commonly, a pitting attack. Pitlocations may result from metallurgical conditions of the steel suraface or soil variations such as rocks, salts, fertilizer, moisture concentration, oxygen concentration, etc. Preventing Corrosion Protecting underground y tanks from corrosion is easily achieved bythe use oftwo commonly applied Protection methods: external coating and cathodic protection. These two methods are complementary and should be used in conjunction with the other. An effective external rotective coating Insulates the steel from the soil environment, thus preventing the flow of corrosion current from the anode to the cathode. Aneffective external coating can protectover99% of the tank surface area. However, no coating is perfect. Damage from construction or soil stresses create tiny defects, which may result in accelerated corrosion atthe defect. Cathodic protection prevents corrosion at those defects by applying DC current from an external source, forcing the tank to become cathode. Application of sufficient DC current to the tank will prevent any corrosion from occurring. The two general types of cathodic protection systems are sacrificial and Impressed current. Sacrificial systems are used when the amount of current required for the protection is small, such as in underground propane tanks. Impressed current systems are more commonly used for large structures such as large diameter Pipelines. Electrical isolation of the tank from metallic piping systems and electrical grounds is critical for the cathodic protection system's effectiveness, How Sacrificial Cathodlc Protection Works Sacrificial systems work by creating a galvanic connection between two different metals. The most common anode material is magnesium, which when coupled to steel results in DC current flow from the magnesium to the steel. The open circuit potential of steel is about -0.50 volts referenced to a copper sulfate electrode. The open circuit potential of magnesium is about -1.55V to-1.80V. By connecting the two metals together, the difference of 1 to 1.25Vvolts results in current flow to the tank that overcomes the natural corrosion cells that exist on the tank. With this current available to the tank, no corrosion occurs, Magnesium Anodes There are a variety of anode sizes and alloys used for cathodic protection. The two primary alloys are designed as H-1 (or AZ63) and High Potential. The H-1 alloy is produced from recycled magnesium and has an open circuit potential of approximately—1.55V. This alloy Is well suited for protection of underground propane tanks. The High Potential alloy is 99% pure magnesium having an open circuit potential up to -1.8V. This alloy should be used for soil applications over 10,000 ohm -cm resistivity. The two most common anode sizes used for underground propane tanks are 9lb. and 171b. The size designation relates to the metal weight 10' of #12 TW Insulated wire is attached to the anodes. Anodes are then backfilled In a mixture of gypsum, bentonite, and sodium sulfate to lower the electrical resistance of the anode to soil. The mixture is a low cost, nonhazardous, electrically conductive backfill. The anode and backfill is then packaged In a cotton bag and either a cardboard box or paper bag. Actual shipping weight of these anodes with backflll Is 27 lb. and 45 lb. Application Recommendations Magnesium anodes can protect underground tanks in most soil conditions, TheH-1 alloy is generally very effective. The following chart Provides size and quantity recommendations forvario us size tanks based on conservative design assumptions. This chart covers soil conditions UP to 10,000 ohm -centimeter resistivity. Resistivities higher than 10,000 ohm-cemimeter generally represent very dry soils, Verification of soil resistivity can be performed through soil analysis. Contact us for design recommendations In locations where soil resistivities exceed 10,000 ohm -cm, or if there Is no effective external coating on the tank. The propane service line from the tank to the house also must be considered in the cathodic protection design, unless the service line Is plastic. All underground steel pipe should be externally coated with a corrosion resistant material. The service line should be electrically isolated at the house with an Insulatingfitting or union. If service pipe is less than 50' fn length, the tank anodes will provide sufficient current to protect both tank and pipe. For longer lengths of pipe, an additional anode maybe required at the house connections. If another metallic material such as copper is used for service piping, the pipe should be electrically isolated from the tank at the fill pipe connection. Copper and steel create a galvanic couple thatwiliaccelerate corrosion of the steel tank when directly connected to copper piping. Generally, copper piping does not require cathodic protection. Soil Type Re it So Is It y? SN Lo ___; Gravel, Rocky Areas Tank Cap, 5000 to 10000 ohm -cm (gal.) s Zp Size Qty. Alloy 120F1bk_1 9f 1 H-1 1509# 1 H-1 250 9d 2 H-1 325 9# 2 H-1 500 9# 2 H-1 10009# 4 H-1 1500 9 a 4 H-1 200094 6 H-1 'Based on 90% effective external coating, 2 ma/n2 current density, and 30- year Anode life. Anode Installation 1. Determine size and quantity of anodes from application chart. 2. When a single anode is Installed, it should be located near the tank center on either side of tank. 3. When multiple anodes are installed, space them evenly around the tank. See examples below. 1 anode 2 anodes 4 anodes 4.Anodes are shipped in either cardboard boxes or multi -wall papersacks. Remove outer container and burythe cloth bagged anode. If anode is supplied in plastic bag, remove plastic bag before installing. 5.Install anodes approximatelytwo to three feetfrom the tank and at least as deep as the center line of the tank. Anodes work best In locations with permanent moisture, so generally the deeper the better. 6.After placing the anode, stretch out the anode connection wire and extend over to a connection point on the tankfill pipe. 7. Cover the anode with approximately six Inches of backfill and pour 5 gallons of water on the anode to saturate the prepared backfill. Water is necessary to activate the anode. 8.Connect the anode wire to the tank with a low electrical resistance connection. Examples are threaded stud on the tank fill pipe or any accessible metallic connection point to the tank. All connections should be coated with a moisture -proof material. 9.Ideally, the tank connection is made in the area of the tank fill pipe within the covered dome. With access to the anode wire, subsequent testing of the tank can include measurement of anode output and verification of performance. 10.Verify performance of the anode using an appropriate test procedure. Mech",_5'al Connection Under Dome Cathodic Protection Testing Procedure Equipment Needed: Digital Voltmeter, Red Test Lead Min.12' Long & Black Lead Min. 2' Long, Reference Electrode (Copper/Copper Sulphate Half -Cell) STEP 1: Using a digital voltmeter insert the red test lead into the Volt jack of the meter and select the 2 or 20 volt DC scale. Clip red test lead connector to an uncoated metallic area of the tank, preferably to the fill pipe multivalve. A good solid connection is very important (DO NOT connect to shroud). STEP 2: Insert the black test lead into the Common jack on the meter, and connect the opposite end of the lead to a charged reference electrode (Yz cell). STEP 3: Remove protective cap from the porous plug at bottom end of electrode. Place porous plug end Into native soil (remove grass if necessary) at four locations around the tank (one on each side of the tank, and one at each end of the tank). If difficulty is encountered obtaining readings, moisten soil with water or dig Y2 cell deeper into the soil. STEP 4: Record all four meter readings on an appropriate form. The least of all four readings should be a minimum of-0.850v or more negative. (Note: If any of the four readings are below (less negative) -0.850v then the tank is not fully protected), Charging Reference Electrode STEP 1: Unscrew and remove porous plug end of new reference electrode. Add deionized or distilled water to the copper sulfate crystals, filling electrode completely. The solution will turn blue in color and there should always be excess crystals at the bottom of the tube. DO NOT USE TAP WATER. STEP 2: Replace porous plug end of electrode and place in an upright position so that the porous plug end is facing in the down position and let stand for 1 hour before use. This will allow the porous plug to become completely saturated before use. Caution: Do not allow electrode to contact all, road salts, or other substances that may contaminate the solution by absorption through porous plug. Do not allow electrode to freeze. Distributed By: Ideal for use as a flrat stage regulator an any domestfo elze p9ME or 007 container In propane gas Installations requidng up to 1,600,000 STU'a per hour. 111 regulator is DOT set in reduce cane gas Pressure to an Intermadiate pressure of approalmalsly 10a Pale,to Provides accurate first stage regulepon In lwa•stgga bulk P'SIndustrla Ifuneoas or boilers. Alec In o pinrated nSO used tmult pled ®rdlllietlg Infaarmation Reduce tank pressure to an burners for applications like when used farnnal stage 70 6.10 MIh NFPppemphleted pie9suM0nGel,mustellharinoetpare�e lnteBrdlrellerY9lVeoreepalete tepervelV68houldhe epecMledln eCEen1B11e6 " Mazmtun naWheeedon Inlet preeeureYO Pala hlgherlhen In^.�...,.,_. __... Designed to reduce drat al1191, e Idealermam i commerais, Installations, Multiple cylinderinstallatfans and normal o many loads , g pressure of 8 to 20 PSIG down to homer pressure, normally 11"wo, sil �ro9eoine� itrs�rsauaiti®s� The LV9403IR= burner pressure Beck Mount Regulator le daslgned to reduce first requirements a nrmaity 11 w,o. Dsslgned as a second stage rag, p to 450 000 BTUIhr, and are ideal for homes, moblie Orderina Ienfor 0aua41®rt Maximum slow based o nurr "' P51G Inletu ,i s n 10 PSIM Inlet and 9^ w,c• dal(very pressure. —uo pressure or 5.10 P816dawn to falor for smaller applicatfons with flow homes, and cottages, Ll