USACE / NAVFAC / AFCESA / NASA UFGS-11 82 21 (August 2008) ---------------------------- Preparing Activity: USACE Superseding UFGS-11 82 21 (October 2007) UFGS-11 82 19 (April 2006) UNIFIED FACILITIES GUIDE SPECIFICATIONS References are in agreement with UMRL dated January 2009 SECTION 11 82 21 MEDICAL WASTE INCINERATORS 08/08 NOTE: This guide specification covers the requirements for furnishing, installing, adjusting, and testing [manually] [automatically] controlled air medical waste incinerators having a capacity ranging from 63 to 252 grams/second (75 to 2000 pounds/hour). Edit this guide specification for project specific requirements by adding, deleting, or revising text. For bracketed items, choose applicable items(s) or insert appropriate information. Remove information and requirements not required in respective project, whether or not brackets are present. Comments and suggestions on this guide specification are welcome and should be directed to the technical proponent of the specification. A listing of technical proponents, including their organization designation and telephone number, is on the Internet. Recommended changes to a UFGS should be submitted as a Criteria Change Request (CCR). This guide specification includes tailoring options for AFCESA, NAVFAC, NASA and USACE. Selection or deselection of a tailoring option will include or exclude that option in the section, but editing the resulting section to fit the project is still required. PART 1 GENERAL NOTE: This packaged incinerator is intended to burn waste materials of biological and pathological nature. 1.1 REFERENCES NOTE: This paragraph is used to list the publications cited in the text of the guide specification. The publications are referred to in the text by basic designation only and listed in this paragraph by organization, designation, date, and title. Use the Reference Wizard's Check Reference feature when you add a RID outside of the Section's Reference Article to automatically place the reference in the Reference Article. Also use the Reference Wizard's Check Reference feature to update the issue dates. References not used in the text will automatically be deleted from this section of the project specification when you choose to reconcile references in the publish print process. The publications listed below form a part of this specification to the extent referenced. The publications are referred to within the text by the basic designation only. AIR MOVEMENT AND CONTROL ASSOCIATION INTERNATIONAL (AMCA)AMCA 210(2007) Laboratory Methods of Testing Fans for Aerodynamic Performance RatingAMCA 99(2003) Standards HandbookAMERICAN SOCIETY OF CIVIL ENGINEERS (ASCE)ASCE 25(2008) Standard for Earthquake-Activated Automatic Gas Shutoff DevicesASCE/SEI 7-05(2006) Minimum Design Loads for Buildings and Other Structures, Including Supplement No. 1AMERICAN WELDING SOCIETY (AWS)AWS B2.1(2005; Errata 2006; Errata 2006) Welding Procedure and Performance QualificationAWS D1.1/D1.1M(2008) Structural Welding Code - SteelASME INTERNATIONAL (ASME)ASME B1.20.1(1983; R 2006) Pipe Threads, General Purpose (Inch)ASME B16.1(2005) Standard for Gray Iron Threaded Fittings; Classes 125 and 250ASME B16.11(2005) Forged Fittings, Socket-Welding and ThreadedASME B16.15(2006) Cast Bronze Threaded Fittings Classes 125 and 250ASME B16.21(2005) Nonmetallic Flat Gaskets for Pipe FlangesASME B16.3(2006) Malleable Iron Threaded Fittings, Classes 150 and 300ASME B16.39(1998; R 2006) Standard for Malleable Iron Threaded Pipe Unions; Classes 150, 250, and 300ASME B16.4(2006) Standard for Gray Iron Threaded Fittings; Classes 125 and 250ASME B16.5(2003) Standard for Pipe Flanges and Flanged Fittings: NPS 1/2 Through NPS 24ASME B16.9(2007) Standard for Factory-Made Wrought Steel Buttwelding FittingsASME B40.100(2005) Pressure Gauges and Gauge AttachmentsASME BPVC SEC IX(2007; Addenda 2008) Boiler and Pressure Vessel Code; Section IX, Welding and Brazing QualificationsASME PTC 19.3(1974; R 2004) Temperature Measurement Instruments and ApparatusASTM INTERNATIONAL (ASTM)ASTM A 1008/A 1008M(2008a) Standard Specification for Steel, Sheet, Cold-Rolled, Carbon, Structural, High-Strength Low-Alloy and High-Strength Low-Alloy with Improved Formability, Solution Hardened, and Bake HardenedASTM A 1011/A 1011M(2008) Standard Specification for Steel, Sheet, and Strip, Hot-Rolled, Carbon, Structural, High-Strength Low-Alloy and High-Strength Low-Alloy with Improved FormabilityASTM A 283/A 283M(2003; R 2007) Standard Specification for Low and Intermediate Tensile Strength Carbon Steel PlatesASTM A 319(1971; R 2006) Standard Specification for Gray Iron Castings for Elevated Temperatures for Non-Pressure Containing PartsASTM A 36/A 36M(2008) Standard Specification for Carbon Structural SteelASTM A 48/A 48M(2003; R 2008) Standard Specification for Gray Iron CastingsASTM A 53/A 53M(2007) Standard Specification for Pipe, Steel, Black and Hot-Dipped, Zinc-Coated, Welded and SeamlessASTM A 653/A 653M(2008) Standard Specification for Steel Sheet, Zinc-Coated (Galvanized) or Zinc-Iron Alloy-Coated (Galvannealed) by the Hot-Dip ProcessASTM A 733(2003) Standard Specification for Welded and Seamless Carbon Steel and Austenitic Stainless Steel Pipe NipplesASTM B 42(2002e1) Standard Specification for Seamless Copper Pipe, Standard SizesASTM B 88(2003) Standard Specification for Seamless Copper Water TubeASTM B 88M(2005) Standard Specification for Seamless Copper Water Tube (Metric)ASTM C 155(1997; R 2007) Standard Specification for Insulating FirebrickASTM C 195(2000) Standard Specification for Mineral Fiber Thermal Insulating CementASTM C 196(2000; R 2005) Standard Specification for Expanded or Exfoliated Vermiculite Thermal Insulating CementASTM C 27(1998; R 2008) Fireclay and High-Alumina Refractory BrickASTM C 270(2008a) Standard Specification for Mortar for Unit MasonryASTM C 401(1991; R 2005) Alumina and Alumina-Silicate Castable RefractoriesASTM C 612(2004e1) Mineral Fiber Block and Board Thermal InsulationASTM D 396(2008b) Standard Specification for Fuel OilsASTM F 1097(1991; R 2006) Mortar, Refractory (High-Temperature, Air-Setting)FM GLOBAL (FM)FM P7825b(2005) Approval Guide Electrical EquipmentISA - INTERNATIONAL SOCIETY OF AUTOMATION (ISA)ISA MC96.1(1982) Temperature Measurement ThermocouplesMANUFACTURERS STANDARDIZATION SOCIETY OF THE VALVE AND FITTINGS INDUSTRY (MSS)MSS SP-70(2006) Standard for Cast Iron Gate Valves, Flanged and Threaded EndsMSS SP-80(2008) Bronze Gate, Globe, Angle and Check ValvesNATIONAL ELECTRICAL MANUFACTURERS ASSOCIATION (NEMA)NEMA MG 1(2007; Errata 2008) Standard for Motors and GeneratorsNATIONAL FIRE PROTECTION ASSOCIATION (NFPA)NFPA 211(2006) Chimneys, Fireplaces, Vents, and Solid Fuel-Burning AppliancesNFPA 31(2006; Errata 2006; Errata 2007) Installation of Oil Burning EquipmentNFPA 54(2008) National Fuel Gas CodeNFPA 82(2004) Incinerators and Waste and Linen Handling Systems and EquipmentU.S. DEPARTMENT OF DEFENSE (DOD)MIL-DTL-15024(Rev F) Plates, Tags and Bands for Identification of EquipmentMIL-STD-461(Rev F) Requirements for the Control of Electromagnetic Interference Characteristics of Subsystems and EquipmentU.S. GENERAL SERVICES ADMINISTRATION (GSA)FS A-A-59222(Basic) Fans, Centrifugal, Draft, Forced and InducedUNDERWRITERS LABORATORIES (UL)UL 50(2007) Standard for Enclosures for Electrical Equipment 1.2 DEFINITION Biological and Pathological Waste is defined as human and animal remains, such as organs, animal carcasses, and solid organic wastes from hospitals, laboratories, slaughterhouses, animal pounds, and similar sources. This type of waste contains up to 85 percent moisture and not more than 5 percent incombustible solids, and has a heating value as low as 2330 kJ/kg 1,000 BTU per pound as fired. 1.3 SYSTEM DESCRIPTION 1.3.1 Site Work Provide site work, structural foundations, and floor slabs as required. 1.3.2 Roof Loads Design roof purlins and beams for dead load plus an additional 0.24 kPa 5 psf uniformly distributed load and an additional 22.4 kN 5000 lb roving concentrated load[; and snow load at [_____] kPa psf plus drift factor where applicable]. Determine wind uplift forces in accordance with ASCE/SEI 7-05 Section 6 using a 100-year recurrence interval and conditions. 1.3.3 Floor Loads Provide operating floors, stairs and access platforms for operation and maintenance, designed for 4.79 kPa 100 psf live load plus dead load. Design equipment platforms for 7.18 kPa 150 psf live load plus a concentrated load of equipment weight at installed location, plus dead load. 1.3.4 Lateral Loads NOTE: Provide seismic requirements for stack and equipment, if a Government designer (either Corps office or A/E) is the Engineer of Record, and show on the drawings. Delete the last bracketed phrase if seismic details are not provided. Pertinent portions of UFC 3-310-04 and Sections 13 48 00 SEISMIC PROTECTION FOR MISCELLANEOUS EQUIPMENT and 13 48 00.00 10 SEISMIC PROTECTION FOR MECHANICAL EQUIPMENT must be included in the contract documents. Include wind and seismic loading in the design. Base design wind pressure on a wind speed of [_____] km/h mph , exposure in accordance with ASCE/SEI 7-05.[ Perform seismic design in accordance with UFC 3-310-04 and Sections 13 48 00 SEISMIC PROTECTION FOR MISCELLANEOUS EQUIPMENT and 13 48 00.00 10 SEISMIC PROTECTION FOR MECHANICAL EQUIPMENT [as indicated] [, and in accordance with ASCE 25 for gas fired equipment].] 1.3.5 Noise Limitations Furnish equipment meeting the noise criteria specified herein through equipment design, acoustic insulation, use of inlet silencers, or other means provided under this contract. Limit sound pressure levels as follows when measured 1525 mm 5 ft from any item of equipment furnished under this contract.          Band Number    Center Band    Maximum Sound Pressure                         Frequency      Level dB, Re 0.0002                              Hz        Microbars   ----------------------------------------------------------------               1             63                 100               2            125                  91               3            250                  84               4            500                  78               5           1000                  78               6           2000                  78               7           4000                  78               8           8000                  78 1.3.6 _{Controls and Instrumentation} a. Include in control equipment and instruments, burners and fan controls, time clocks, relays, operating switches, indicating lights, gauges, motor starters, fuses, alarms, and circuit elements of the control system, and other controls and instruments necessary for unit operation, with system in accordance with the FM P7825b. b. Mount the controls and instruments on one or more free-standing control panels conveniently located to the incinerator, and placed to allow operating personnel effectively monitor incinerator operations. Provide contol system with [on-off control] [proportioning control of the primary air supply and fuel supply to the secondary burner], and temperature indicator controllers or other indicators providing a visual indication for safe loading of the incinerator and excessive high temperature conditions which may require control by the operator. Interlock automatic control circuit systems and manual switches to prevent hazardous conditions or the discharge of excessive amounts of air pollutants. 1.3.6.1 Control Panel Provide a sheet steel, weathertight panel, conforming to UL 50. Provide [a heater to prevent condensation] [NEMA 4 control panels for outdoor installations with electric strip heaters for condensation control.] Flush mount all controls, instruments, and other equipment at the factory and test the assembly prior to shipment. Furnish a lock and 2 keys. All controls and instruments shall be identified with nameplates. 1.3.6.2 Draft Gauges Provide draft gauges conforming to ASME B40.100 with a diaphragm or bellows actuating system, a circular scale, a zero adjusment screw, and suitable shutoff cocks. 1.3.6.3 Pressure Gauges Provide pressure gauges conforming to ASME B40.100, pressure detecting class, single Bourdon tube style, suitable for detecting air pressure. 1.3.6.4 Thermocouples Provide sensors conforming to ISA MC96.1, Type K, in the combustion chamber or as otherwise directed, with a thermocouple suitable for continuous operation and control at temperatures up to 1260 degrees C 2300 degrees F accurate to 0.75 percent, of sufficient length to be inserted 150 mm 6 inches into the furnace. Provide the thermocouple with an adjustable flange and a high-temperature metal alloy, closed-end, protecting tube suitable for insertion into the furnace without support of the projecting end. Supply thirty meters onee hundred feet of 1.52 mm 16-gauge compensating lead wire with a weatherproof braid for connecting the thermocouple to the instrument, so that the installed unit indicates gas passage temperatures and controls burner operation. 1.3.7 Operating Tools Provide and locate as indicated, operating and firing tools, such as shovel or coal scoop, hoe, rake, slice bar with metal handles, regularly used for firing and cleaning incinerators, and a firing tool rack. Provide steel rack, including hooks and other appropriate means for storing the tools in a neat manner. 1.4 SUBMITTALS NOTE: Review submittal description (SD) definitions in Section 01 33 00 SUBMITTAL PROCEDURES and edit the following list to reflect only the submittals required for the project. Submittals should be kept to the minimum required for adequate quality control. A “G” following a submittal item indicates that the submittal requires Government approval. Some submittals are already marked with a “G”. Only delete an existing “G” if the submittal item is not complex and can be reviewed through the Contractor’s Quality Control system. Only add a “G” if the submittal is sufficiently important or complex in context of the project. For submittals requiring Government approval on Army projects, a code of up to three characters within the submittal tags may be used following the "G" designation to indicate the approving authority. Codes for Army projects using the Resident Management System (RMS) are: "AE" for Architect-Engineer; "DO" for District Office (Engineering Division or other organization in the District Office); "AO" for Area Office; "RO" for Resident Office; and "PO" for Project Office. Codes following the "G" typically are not used for Navy, Air Force, and NASA projects. Choose the first bracketed item for Navy, Air Force and NASA projects, or choose the second bracketed item for Army projects. Government approval is required for submittals with a "G" designation; submittals not having a "G" designation are for [Contractor Quality Control approval.] [information only. When used, a designation following the "G" designation identifies the office that will review the submittal for the Government.] Submit the following in accordance with Section 01 33 00 SUBMITTAL PROCEDURES: _{SD-02 Shop Drawings Detail Installation Drawings}[; _G][; _{G, [_____]}] _{SD-03 Product Data}[; _G][; _{G, [_____]}] _Incinerator[; _G][; _{G, [_____]}] _{Controls and instrumentation SD-06 Test Reports Instrument readings}[; _G][; _{G, [_____]}] _Performance[; _G][; _{G, [_____]}] _{Adjusting and Testing}[; _G][; _{G, [_____]}] _{SD-07 Certificates Incinerator}[; _G][; _{G, [_____]}] _{SD-10 Operation and Maintenance Data Operating and Maintenance Instructions}[; _G][; _{G, [_____]}] _{Data Package 4}[; _G][; _{G, [_____]}] 1.5 QUALITY ASSURANCE 1.5.1 Asbestos Prohibition Asbestos and asbestos-containing products are prohibited. 1.5.2 _{Detail Installation Drawings} Submit detail installation drawings for the incinerator, foundation, stack, waste feed system, [heat recovery boiler,] [acid gas scrubber,] [mercury and dioxin control equipment,] fuel burning equipment, ash removal system, flue gas cleaning system, and controls. Include in detail drawings all equipment settings and connections, complete electrical wiring, controls, and connection diagrams and indicate clearances required for maintenance and operation. 1.5.3 Welding Perform all welding in accordance with ASME BPVC SEC IX and AWS D1.1/D1.1M by welders certified to have passed qualification tests using procedures covered in AWS B2.1. 1.5.4 Special Tools Furnish all special tools for assembly, adjustment, setting, or maintenance of equipment specified as standard accessories. 1.6 DELIVERY, STORAGE, AND HANDLING Protect all equipment delivered and placed in storage from the weather, humidity and temperature variations, dirt and dust, or other contaminants. 1.7 EXTRA MATERIALS Submit spare parts data for each different item of material and equipment specified, after approval of detail drawings, and not later than [_____] months prior to date of beneficial occupancy. Include a complete list of parts and supplies, with current unit prices and source of supply, and a list of the spare parts recommended by the manufacturer to be replaced after [1] [and] [3] year[s] of service. PART 2 PRODUCTS 2.1 MATERIALS AND EQUIPMENT NOTE: Catwalk, ladder, and guardrail, if required, will be indicated on drawings. Provide materials and equipment which are the standard products of a manufacturer regularly engaged in the manufacture of the product and that essentially duplicate items that have been in satisfactory use at least 2 years prior to bid opening. a. Submit manufacturer's product data, catalog cuts, illustrations, schedules, performance charts, instructions, brochures, diagrams, sound level data, calculations for gas retention times, combustion and air emissions data, and other information to verify compliance with requirements of the contract documents. b. Provide each major component of equipment with the manufacturer's name, address, type or style, model or serial number, and catalog number on a plate secured to the equipment.[ Provide identification conforming to MIL-DTL-15024.] c. Enclose or guard belts, pulleys, chains, gears, couplings, projecting setscrews, keys, and other rotating parts located where any person may come in close proximity thereto. Guard and cover high-temperature equipment and piping located where they could endanger personnel or create a fire hazard with insulation of type specified for service. d. Provide items such as a [catwalk,] [stair,] [ladder,] [and guardrail] where shown and in accordance with Section [05 50 13 MISCELLANEOUS METAL FABRICATIONS] [05 50 14 STRUCTURAL METAL FABRICATIONS] [ 05 51 33 METAL LADDERS]. f. Provide materials and equipment conforming to the following: 2.1.1 Mortar ASTM C 270. 2.1.2 Brick 2.1.2.1 Firebrick ASTM C 27. Interpreted to include straight, radial, wedge, and skew-type brick, cupola blocks, and other similar shapes. 2.1.2.2 Insulating Firebrick ASTM C 155. 2.1.3 Castings, Gray Iron ASTM A 48/A 48M. 2.1.4 Tubing, Copper, and Fittings ASTM B 88M ASTM B 88, Type K; fittings, flare type, cast brass, or wrought copper. 2.1.5 Mortar, Firebrick ASTM F 1097. 2.1.6 Pipe and Fittings 2.1.6.1 Gaskets Provide nonasbestos compressed material gaskets in accordance with ASME B16.21, 2 mm 1/16 inch thickness, full face or self-centering flat ring type; containing aramid fibers bonded with styrene butadiene rubber (SBR) or nitrile butadiene rubber (NBR). Use NBR for hydrocarbon service. 2.1.6.2 Cast-Iron Flanges and Flanged Fittings ASME B16.1, Class 125 or 250 as required to match adjacent piping. 2.1.6.3 Nipples ASTM A 733, standard weight. 2.1.6.4 Pipe ASTM A 53/A 53M, Type S, Grade A, standard weight; or copper pipe, ASTM B 42. 2.1.6.5 Pipe Fittings a. Steel: Provide buttwelding fittings conforming to ASME B16.9; socket welding fittings conforming to ASME B16.11; and flanged fittings conforming to ASME B16.5. b. Brass or Bronze: ASME B16.15, Class A, 862 kPa 125 psi. c. Cast-Iron: ASME B16.4, 862 kPa 125 psi, type to match adjacent piping. d. Malleable-Iron: ASME B16.3, type to match adjacent piping. 2.1.6.6 Unions ASME B16.39, Malleable Iron threaded pipe unions, Class 150, 250, or 300 as indicated or required for service. 2.1.7 Pipe Threads ASME B1.20.1. 2.1.8 Galvanized Steel Sheets ASTM A 653/A 653M for incinerator casings, housing, and components. Gauges specified are United States Standard Sheet and Plate Gauge. 2.1.9 Steel Sheets and Strips ASTM A 1008/A 1008M or ASTM A 1011/A 1011M, for incinerator casings, housings, and components. 2.1.10 Thermometers ASME PTC 19.3, with wells and temperature range suitable for the use encountered. 2.1.11 Valves 2.1.11.1 Angle MSS SP-80, Type 1, 2, or 3, Class 125 as required. Provide iron-body valves in sizes above 75 mm 3 inches with brass or bronze standard trim and glands or followers in the stuffing boxes. Provide valves with nonmetallic renewable composition discs and raised flat seats designed for 862 kPa 125 psi steam. Secure iron wheels with hexagonal nuts. 2.1.11.2 Check MSS SP-80, Type 1, 2, 3, or 4, Class 125, as required. Provide iron-body check valves in sizes above 75 mm 3 inches of the swing type designed for 862 kPa 125 psi steam, and check valves with renewable composition discs or metallic discs of the regrinding type to permit regrinding without removing valve from the line. 2.1.11.3 Gate Sizes of 40 mm 1-1/2 inches or less, MSS SP-80, Class 125, Type 1 and 2; 50 mm 2 inch size and over, MSS SP-70 , Class 125 or 250, design OT or OF, as required. 2.1.11.4 Globe MSS SP-80, Type 1, 2, or 3, Class as required. Provide iron-body globe valves in sizes above 75 mm 3 inches with brass or bronze standard trim and glands or followers in the stuffing boxes. Provide valves with nonmetallic renewable composition discs and raised flat seats designed for 862 kPa 125 psi steam. Secure iron wheels to the stems with hexagonal nuts. 2.1.12 Refractory for Castings ASTM C 401, Class R. Provide hydraulic setting refractory of a type especially suitable for incinerators required to burn wet material. 2.1.13 Charging Ram Provide hydraulically operated, self-contained ram mechanism with directional control, capable of injecting small loads of refuse at frequent intervals to ensure relatively uniform burning rates in addition to limiting the amount of air entering the primary chamber with each charge; [continuously] [intermittently] moving the burning waste toward the cleanout area. 2.1.14 Pyrometer Provide indicating recording pyrometer for measuring incinerator temperature, with a temperature range from minus 18 to plus 1315 degrees C 0 to 2400 degrees F accurate to within plus or minus 1 percent of the range. 2.1.15 Thermocouple Provide thermocouples indicating gas passage temperatures and control of burner operation, suitable for operation up to 1260 degrees C2300 degrees F and accurate within 0.5 percent of the operating and indicating temperature range. 2.2 ELECTRICAL WORK NOTE: Indicate the type and class of motor enclosure depending on the environment in which the motor is to be used. Provide electrical motor-driven equipment as specified, complete with motorsconforming to NEMA MG 1, motor starters, and controls[ conforming to MIL-STD-461], with enclosures as indicated. Provide electrical equipment, including motors and wiring, in accordance with Section 26 20 00 INTERIOR DISTRIBUTION SYSTEM, with electrical characteristics as indicated or specified. Provide motor starters complete with thermal overload protection and other appurtenances necessary for the motor control specified, and of sufficient size to drive the equipment at the specified capacity without exceeding the nameplate rating of the motor. Provide manual or automatic control, protective or signal devices required for the operation specified, and any control wiring required for controls and devices specified but not shown. 2.3 _INCINERATOR NOTE: The incinerators are capable of burning medical waste. The composition of Type 4 waste is indicated in the following table: WASTE VS. CONTENT                     Noncombustible      Moisture       Heating Value                     Solids (Max %       Content        J/kg                     by Weight)          (Max %)        (BTU Per Pound) Type ------------------------------------------------------------------------- (Highly Combustible)     5                   10        19,771,000 (8,500) (Pathological)           5                   85         2,326,000 (1,000) The medical waste to be disposed of in the incinerator is a mixture of paper, plastics, Type 4 waste, etc., and is of a widely varying nature with a Btu content which may well exceed the usually reported value of 2,326,000 J/kg (1000 Btu per pound). Prior to developing final design of the incinerator, detailed waste classification should be made in consultation with U.S. Army Center For Health Promotion & Preventive Medicine, Aberdeen Proving Ground, Maryland. Include the ranges of amounts of glass, metal, paper, plastics, organic, rubber, cloth, wood, moisture, etc., in the waste and the variable joule (Btu) content. The waste stream at each installation must be analyzed and the information should be utilized for the final design. Provide an incinerator with a solid hearth in the primary combustion chamber where partial burning and conversion of the combustible organic matter occurs, and a secondary combustion chamber that consumes the combustible gases and entrained combustible particles, with gas-tight shell construction. Provide an incinerator suitable for [indoor installation] [outdoor installation, including totally enclosed electric motors, and corrosion and moisture protection,] and equipped for [manual] [mechanical] [automatic] charging and operation. Incinerator shall be a complete package-type unit, factory fabricated and assembled; operating under negative air pressure and ready for attachment of all utility connections. 2.3.1 Type of Waste Provide an incinerator capable of burning typical medical waste including paper, plastics of various kinds, and a small fraction of Type 4 (pathological) waste. 2.3.2 Capacity Provide incinerator with a capacity of not less than [_____] kg pounds per hour, based on [operating the incinerator no more than 6 to 8 hours continuously per day.] [burning medical waste parts which have a water content as high as 85 percent by weight.] [Design for daily ash clean-out for systems designed to operate no more than 6 to 8 hours continuously.] 2.3.3 Volume NOTE: Fill in the blanks to indicate minimum volumes. Consult manufacturers of medical waste incinerators for furnace and chamber volumes to satisfy the capacity specified. Provide furnace with an inside volume , exclusive of the space occupied by the refractory hearths and walls, of not less than [_____] cubic meters feet; with a primary combustion chamber volume above the burning hearth of not less than [_____] cubic meters feet, and a final combustion settling chamber volume of not less than [_____] cubic meters feet. 2.3.4 System Components NOTE: The component list contains items of equipment designed to reduce emissions which must be evaluated against federal, state, and local regulatory requirements. Other items of equipment must be evaluated for cost effectiveness. Provide a complete waste burning system including combustion air fan, primary and secondary burners, air distribution and burner controls, ducts, breeching, stack, [bottom ash conveyor and collection,] [feed rams,] [[fire tube] [water tube] heat recovery boiler and emergency bypass stack,] [[venturi] [packed tower] wet scrubber,] [dry scrubber,] [dry powdered activated carbon injection system,] [[urea] [ammonia] injection system,] [acid gas reagent storage vessels,] [carbon storage vessels,] [combined acid gas reagent and carbon storage vessels,] [air compressors,] [slurry pumps,] [water pumps,] [baghouse,] [[vacuum type] [enclosed mechanical type] fly ash collection system,] control and emission monitoring equipment. 2.4 OPERATING AND PERFORMANCE REQUIREMENTS 2.4.1 Weight Reduction NOTE: Indicate the effectiveness and burnout capability of the incinerator to be provided (15 percent ash is a reasonably accepted figure). Provide an incinerator capable of reducing waste to an ash not to exceed [_____] percent of the total combustible charges when tested as specified. 2.4.2 Stack Discharge NOTE: Review all applicable federal, regional and local emission regulations and utilize the most stringent requirements. Typical values are as follows (all emission limits will be corrected to 7 percent oxygen, dry basis): Carbon Monoxide (CO): 50 ppmv, 12-hour average as measured by a Continuous Emissions Monitoring System (CEMS); Particulate Matter: 0.013 gr/dscf (30 mg/dscm) as measured by EPA Reference Method 5; Opacity: 5 percent, 3-minute average as measured by a CEMS; Sulphur Dioxide (SO2): 45 ppmv, 12-hour average as measured by a CEMS; Nitrogen Oxides (NOx): 210 ppmv, 12-hour average as measured by EPA Reference Method 7; Hydrogen Chloride (HCL): 42 ppmv, or 97 percent reduction, 9-hour average as measured by EPA Reference Method 26; Total Hydrocarbons: 70 ppmv, 1-hour average as measured by EPA Reference Method 25; Mercury: 210 gr/106dscf (0.47 mg/dscm) or 85 percent reduction, 12-hour average as measured by EPA Reference Method 29; Lead: 44 gr/106dscf (0.10 mg/dscm), 12-hour average as measured by EPA Reference Method 29; Cadmium: 22 gr/106dscf (0.05 mg/dscm), 12-hour average as measured by EPA Reference Method 29; Dioxin/Furans: 35 gr/109dscf (1.9 ng/dscm) toxic equivalency of 2, 3, 7, 8-TCDD, 12-hour average as measured by EPA Reference Method 23. Provide pollution control equipment meeting or providing lower emission values than those specified for the following: a. Carbon Monoxide (CO): [_____] ppmv, 12-hour average as measured by a Continuous Emissions Monitoring System (CEMS); b. Particulate Matter: [_____] gr/dscf ([_____] mg/dscm) as measured by EPA Reference Method 5; c. Opacity: [_____] percent, 3-minute average as measured by a CEMS; d. Sulphur Dioxide (SO2): [_____] ppmv, 12-hour average as measured by [a CEMS] [EPA Reference Method [_____]]; e. Nitrogen Oxides (NOx): [_____] ppmv, 12-hour average as measured by EPA Reference Method 7; f. Hydrogen Chloride (HCL): [_____] ppmv, or [_____] percent reduction, 9-hour average as measured by EPA Reference Method 26; g. Total Hydrocarbons: [_____] ppmv, 1-hour average as measured by EPA Reference Method 25; h. Mercury: [_____] gr/106dscf ([_____] mg/dscm) or [_____] percent reduction, 12-hour average as measured by EPA Reference Method 29; i. Lead: [_____] gr/106dscf ([_____] mg/dscm), 12-hour average as measured by EPA Reference Method 29; j. Cadmium: [_____] gr/106dscf ([_____] mg/dscm), 12-hour average as measured by EPA Reference Method 29; k. Dioxin/Furans: [_____] gr/109dscf ([_____] ng/dscm) toxic equivalency of 2, 3, 7, 8-TCDD, 12-hour average as measured by EPA Reference Method 23; Correct all emission limits to 7 percent oxygen, dry basis. The following definitions were used above: parts per million by volume (ppmv); dry standard cubic feet (dscf); dry standard cubic meters (dscm); grams (gr); milligrams (mg); and nanograms (ng). 2.4.3 Noise Noise level at 305 mm 1 foot from any incinerator component shall not exceed 85 dBA. Provide sound dampening devices on equipment as required. 2.5 FURNACE CONSTRUCTION 2.5.1 Primary Chamber Construct the primary chamber with a steel casing supported by a steel frame, and provide with insulation and refractory. Make the casing with 2.66 mm 12-gauge sheet steel minimum, conforming to ASTM A 1011/A 1011M and reinforced to withstand internal pressures without deflection or damage to refractory or other components of the incinerator. Construct the frame and all reinforcing members of steel conforming to ASTM A 36/A 36M. Provide a free-standing frame capable of supporting the weight of all components of the incinerator, including doors, burners, breeching, stack connections, and appurtenant assemblies without binding or warping. Make the frame and casing of all welded construction, completed and erected prior to installation of the refractory and insulation. Perform all welding in accordance with ASME BPVC SEC IX and AWS D1.1/D1.1M. Provide all access doors and parts with seals to prevent emission of smoke or admission of significant amounts of air during incinerator operation, and a primary chamber with no openings which would permit leakage of waste fluids. 2.5.2 Secondary Chamber Provide a secondary chamber with an exterior casing not less than 2.66 mm 12-gauge sheet steel conforming to ASTM A 1011/A 1011M, with insulation and refractory lining of the same class, type, and thickness required for walls in the primary chamber. Allow for a minimum dwell time of [0.5] [0.8] [1.0] seconds for any condition within normal operating limits. 2.5.3 Insulation Provide insulation conforming to ASTM C 612, Class 5 and designed to be used with masonry or reinforced concrete or noncombustible material, with a fire resistant rating of not less than 3 hours, to prevent damage to the foundation from excessive heat. As a minimum, provide insulation thickness to limit the temperature of the outer casing to 66 degrees C 150 degrees F maximum in an ambient temperature of 21 degrees C 70 degrees F when the unit is operating at full-rated capacity. Use insulating cement conforming to ASTM C 195 or ASTM C 196. 2.5.4 Refractory Provide heat-resistant plastic super-duty fireclay refractory conforming to ASTM C 27. The minimum thickness of plastic or castable refractory is 110 mm 4-1/4 inches for walls and [110] [64] mm [4-1/4] [2-1/2] inches for hearths. Attach refractory walls to the casing with alloy steel or refractory anchors to form a monolithic structure which will resist heat and support the walls with a safety factor of 4. Prevent bulging and destruction of refractory due to heat stress by reinforcing, expansion joints, ties, and anchors. 2.5.5 Exterior Walls Provide 2.66 mm 12-gauge sheet steel walls reinforced with steel framing [and] [,] provided with door frames [, and mounted on structural steel skids]. 2.5.6 Hearth Provide an abrasion resistant refractory hearth constructed of heat-resistant, thermal-insulating clay conforming to ASTM C 401, Class R plastic or castable type, high-duty class, capable of supporting not less than twice the hourly burning rate and preventing leakage of waste fluids. 2.5.7 Doors NOTE: Select door material to be employed (many manufacturers recommend steel). a. Provide doors for stoking, cleanout, and charging areas, with securely attached door frames. Construct doors and frames of [cast iron conforming to ASTM A 319] [steel conforming to ASTM A 1011/A 1011M or ASTM A 36/A 36M]. Line doors, exposed to flame or direct heat of combustion gases, with the same type and thickness of refractory and insulation used in the combustion chamber. b. Secure refractory to the doors so as to prevent sagging. Taper refractory edges to clear door frames during movement of swinging doors. Weld alloy steel hooked bars to door cover to anchor the refractory, to enable safe operation by one person, and maintaining temperature of door handles to permit operation of doors without gloves or other protective devices. c. Interlock charging doors with primary burners and air supply so that burner ignition shuts off and underfire air dampers close when doors open. Gasket door closure with nonasbestos packing. d. [Provide counter-weights for vertically operated doors requiring a maximum manual operating force of 133 N 30 pounds maximum.] [ Provide guillotine-type doors which lift completely off the seals to effect opening.] [Provide full-swing-type doors with an integral smaller feed door having a minimum rectangular clear opening of 610 by 610 mm 24 by 24 inches or a minimum circular clear opening of 762 mm 30 inches diameter.] Include hasps or brackets for doors to permit locking. 2.5.7.1 Stoking and Cleanout Doors Provide tight fitting cleanout doors which allow access for total cleanout, visual inspection of the entire interior of the incinerator, and prevent leakage of waste fluids. 2.5.7.2 Mechanical-Charging Doors Provide inner and outer [guillotine] [swing] [automatic sliding] mechanical-charging doors type, with the inner or charging door opening with operation of the charger. Interlock the inner and outer doors to prevent simultaneous opening during incinerator operation. Insulate and line the combustion chamber door with refractory material. Construct the outer door of the same materials as the exterior casing of the incinerator. Doors shall be provided with means for manual operation. 2.5.8 Observation Ports Provide two observation ports, 75 mm 3 inches in diameter, on the charging door for viewing the primary combustion chamber during operation. Construct observation ports of black steel or cast-iron tube or duct having a minimum thickness of 3.42 mm 10 gaugeand provided with heat-resistant glass cover, or an angular steel frame and closure plate with handle, for operation without gloves or other protective devices. Extend the tube or duct from the exterior of the casing to not less than one-half the thickness of the refractory lining, and weld the frame to the casing, to provide a gas-tight refractory opening. 2.5.9 Damper Provide a controller actuated refractory lined damper which regulates secondary, underfire, and overfire air, constructed of steel conforming to ASTM A 1011/A 1011M, not less than 1.52 mm 16-gauge thick, operating without noise or flutter, and [pneumatically operated] [electric motor operated at [_____] volt ac] actuators. 2.5.10 Bypass Dampers NOTE: Use a maximum leakage rate of 1.0 percent. Review all applicable emission requirements and percent reductions to determine an acceptable leakage rate. Construct bypass dampers to provide a leakage rate of less than [_____] percent at 1.5 times the maximum operating pressure. 2.5.11 Test Holes and Test Groups NOTE: Indicate and clearly identify an instrument test group near every thermocouple well to connect portable equipment to verify installed equipment. Provide test holes, near the test group shown on the contract drawings, and fit with standard weight, 50 mm 2 inch diameter, black steel pipe welded to the casing. Extend the sleeve from the exterior of the casing to not less than one-half the thickness of the refractory lining. Form the refractory opening from the end of the pipe sleeve to the interior wall surface to shield the end of the sleeve from reflected heat, and fit with a brass screw cap. Submit a copy of the _{Instrument Readings} to the Contracting Officer. 2.6 FLUE GAS CLEANING SYSTEM NOTE: Where particulate control is required at the levels specified in paragraph: STACK DISCHARGE, specify dry type adsorber. Provide a complete flue gas cleaning system (FGC)consisting of a [[dry] [semi-dry/semi-wet] [wet] powdered activated carbon injection system, and a [dry] [semi-dry/semi-wet] [wet] acid gas scrubber system] [combination [dry] [semi-dry/semi-wet] [wet] powdered activated carbon and acid gas scrubbing system] [and [baghouse] [precipitator] for particulate control]; capable of [continuous operation] [operation compatible with the incineration capacity and schedule specified]. 2.6.1 System Components Provide each scrubber system with bulk storage silos, unloading facilities for trucks, dust control filters, mixing equipment, slurry tanks, pumps, compressors, induced draft fans, and all piping and valves necessary to provide a complete and operating system. 2.6.2 Product Storage Capacity Provide bulk storage capacity for all required products to sustain a minimum operating period of [two] [_____] weeks between deliveries. 2.6.3 Adsorbers 2.6.3.1 Access Provide access openings at strategic locations for inspection, cleaning, and maintenance, all being a gas tight quick-opening type. Elevate the adsorbers to permit 2130 mm 7 feet access under the lowest point which would collect particulates. Locate an access door at this lowest point to permit removal of accumulated particulate; designed to open with an accumulation of material above it. 2.6.3.2 Construction Construct adsorber with at least 4.76 mm 3/16 inch thick steel plate, ASTM A 36/A 36M or ASTM A 283/A 283M, grades B, C, or D. Space external stiffeners as required to provide support for the vessel skin. Seal weld all structurally welded seams. Design joints to be assembled air and water tight. Design adsorber for a gas pressure of plus or minus 635 mm 25 inch water gage, or as required by the system operation, whichever is greater, and with any panel deflection not exceeeding L/240. 2.6.3.3 Gas Flow Provide the gas inlet to each module with internal deflector plates designed to provide uniform gas distribution and velocities through the unit. 2.6.4 Product Handling and Preparation System Provide a complete system to receive, store, and supply [product] [lime] to the spray-dry adsorbers, with the capability of supplying sufficient [product] [lime] for the incinerator operating at 120 percent of full load. Include in the system, but do not limit to, [product] [lime] storage silo complete with vibrating bin discharger, flexible connections, gravimetric feeders, attrition slaker, [product] [lime] slurry and water pumps, slaked [product] [lime] storage tank, and agitators. 2.6.5 Powdered Activated Carbon Provide powdered activated carbons (PAC) specifically made for the removal of mercury, dioxins, and furans with a high percentage of pore sizes in the 20 to 50 angstrom range, with PAC completely devolatilized. 2.6.6 Pebble Quick Lime Analysis Provide flue gas cleaning equipment capable of meeting emission requirements specified using lime with the following composition: SiO2 2.6 percent Al203 0.5 percent Fe2O3 0.4 percent MgO 5.7 percent S 0.03 percent CaO 90.8 percent Available CaO 85.0 percent Fineness 19 mm 3/4 inch x 0 Weight Density 7853 N/cubic meter 50 lb/cubic foot Mass Density 800 kg/cubic meter 1.55 slugs/cubic foot 2.6.7 Service and Process Water Analysis The service and process water analysis will vary; however, consider the following characteristics to be typical: Calcium [_____] ppm Magnesium [_____] ppm Sodium [_____] ppm Bicarbonate [_____] ppm Sulfate [_____] ppm Chloride [_____] ppm Silicon [_____] ppm Iron (as Fe3) [_____] ppm Manganese (as Mn) [_____] ppm Hardness (CaCO3) [_____] ppm pH [ranges between [_____] and [_____]] [is [_____]] 2.7 HEAT RECOVERY BOILER Provide heat recovery boilers in accordance with Section 23 52 43.00 10 HEAT RECOVERY BOILERS 23 52 43.00 20 LOW PRESSURE WATER HEATING BOILERS (UNDER 800,000 BTU/HR OUTPUT). 2.8 AUXILIARY EQUIPMENT 2.8.1 Charging Method Charge the unit [mechanically] [manually]. [Provide a mechanical charger, including an inner door to the combustion chamber, and an outer door to discharge the contents of the loading and holding chamber into the combustion chamber. Provide the charger with a manual control, and an adjustable timer to permit semiautomatic charging at not less than 10-minute intervals. Also provide an interlock to prevent operation of the charger when a predetermined safe operating temperature is exceeded. Locate the charger on the [end] [side] [top] of the incinerator.] [Include a front loading door with minimum dimensions of 610 by 610 mm 24 by 24 inches on the manual charger, with a combustion chamber operating at negative pressure when the loading door is open to prevent injury to the operator and the escape of smoke and gases.] [Provide a hopper-type chamber for top loading chargers.] Provide charging chambers with a capacity of not less than [0.4] [0.8] [_____] cubic meters [0.5] [1.0] [_____] cubic yards. 2.8.2 Burners NOTE: Select values of minimum burner input capacity as indicated in the following table and applicable data inserted within the brackets.                        Size of Burners, kW (1000 Btuh)              --------------------------------------------------------              Capacity of              Incinerator              Type 4              All Types              kg/hr (lb/hr)            Refuse              Refuse              --------------------------------------------------------                   11.3 (25)            87.9 (300)         29.3 (100)                   22.7 (50)           131.9 (450)         58.6 (200)                   34.0 (75)           190.5 (650)         73.3 (250)                   45.4 (100)          249.1 (850)         87.9 (300) a. Provide [gas] [oil] [combination gas and oil] [LPG] burners for the primary and secondary combustion chambers, with each burner as a complete assembly including fuel and control systems, and accessories. Provide a primary burner with an input capacity of not less than [_____] W Btuh, and a secondary burner with a minimum capacity of [_____] W Btuh, capable of maintaining a minimum continuous temperature in the secondary chamber of 871 degrees C 1600 degrees F, and a minimum continuous temperature of 760 degrees C 1400 degrees F at the roof near the exit of the primary chamber. b. Provide electrically spark-ignited burners regulated by a variable set point indicator-controller adjustable from minus 18 to 1371 degrees C minus 27 to 2500 degrees F to operate within the temperature limits recommended by the manufacturer. c. Provide controllers actuated by a thermocouple or shielded bimetallic sensor, with the mounting, flame shape, and characteristics of each burner suitable for the incinerator chamber in which the burner is installed. Flame impingement on the incinerator wall is not permitted. d. Provide each burner with FM P7825b listed and approved flame failure protection. Sight the flame safeguard sensor to detect only the burner flame for which it is designed, with burners which are easily moved out of firing position for inspection, cleaning, adjustment, and maintenance. Locate thermocouples in the primary and secondary chamber, suitable for a maximum temperature of 1260 degrees C 2300 degrees F. Provide a continuous secondary burner which modulates from high to low fire, based on the temperature of the secondary chamber. Provide an on/off firing burner in the primary chamber. 2.8.3 Fuel Oil Storage Tank Provide a fuel oil storage tank, fuel oil conforming to ASTM D 396, and tanks in accordance with Section 33 56 10 FACTORY-FABRICATED FUEL STORAGE TANKS. 2.8.4 Stack NOTE: Depending on requirements at location and personnel involved, temperature of the casing can be 66 to 93 degrees C (150 to 200 degrees F). Limit the casing temperature to 49 degrees C (120 degrees F) maximum when personnel safety is involved. Designer must consider the effect of stack location on adjacent occupied buildings and fresh air intakes. EPA has guidance on stack heights. a. Provide a sectional, circular cross section exhaust stack of the type, size, and number of sections in accordance with the requirements of the stack and refractory manufacturer to adequately support the refractory lining, permit expansion, and prevent cracking of the refractory; conforming to NFPA 211. Secure the refractory to the casing by steel anchors. b. Attach a corrosion-resistant steel spark arrestor fabricated of 1.21 mm 18-gauge, 13 mm 1/2 inch mesh wire screen to the top of the stack. Provide a corrosion-resistant steel weather cap. The temperature of the casing shall not exceed [_____] degrees C degrees F in an ambient temperature of 21 degrees C 70 degrees F. Provide adequate support for any stack installed on top of the incinerator, without placing any of the load on the refractory walls of the incinerator. 2.8.5 Breeching Provide connectors to connect the incinerator to the stack unless the stack is attached directly to the incinerator, in accordance with NFPA 211. Locate the connector at a minimum clear vertical distance of 2450 mm 8 feet above the floor. 2.8.6 Draft Equipment Provide equipment which supplies the correct amount of air to permit complete controlled combustion. Include forced draft fans, draft gauges, dampers, damper actuators, linkage, and appurtenances necessary to maintain a negative draft in primary chamber in order to provide optimum performance at all operating rates. 2.8.6.1 Air Ducts Introduce combustion underfire air to the primary chamber below the waste material through [perforated air pipes] [ducts] [slots located along the side of the hearth]. Control overfire air with [manually] [automatically] controlled air intake ports in the back wall, for completing combustion of combustible materials into gases, or for reducing operating temperatures. Provide dampers to set the air for the proper burning of the waste materials. Size ducts to minimize pressure drops, constructed of sheet steel conforming to ASTM A 1011/A 1011M, with all seams and connections air tight. 2.8.6.2 Fan Provide a fan capable of delivering [_____] cubic meters feet of air against a static head of [_____] mm inches of water at an atmospheric temperature of 16 degrees C 60 degrees F and a barometric pressure of 101 kPa 14.7 psi, centrifugal type with [backward-curved] [forward-curved] [radial-tip] blades, and statically and dynamically balanced fan wheels. Comply with the fan standards of AMCA 99, and FS A-A-59222, applicable to centrifugal furnace fans, rated for flow rate, pressure, power, speed of rotation, and efficiency in accordance with AMCA 210. Provide induced draft fans, where required, designed for handling hot flue gas at the maximum outlet temperature of the incinerator. Provide induced draft fan housings with drain holes to accommodate the drainage of condensation, [air-cooled] [water cooled] drat fan bearings, and fan scroll sheets and rotor blades with protective liners. 2.8.7 Ash Removal Provide the unit with provisions for [manual] [automatic] removal of the ash through the cleanout door upon completion of the burnout and cool-down cycles. Ash removal shall be as indicated for use with portable containers. 2.9 PAINTING AND FINISHING 2.9.1 Treatment Clean the inner surfaces of the outer casing of the incinerator, the exterior surfaces of the outer casing, the control panel, and piping, except corrosion-resistant steel, to base metal for removal of oil and rust before primer is applied at the factory. 2.9.2 Factory Painting Factory paint equipment and component items with the manufacturer's standard finish. Provide a weather resistant finish on all items located outside the building. PART 3 EXECUTION 3.1 EXAMINATION After becoming familiar with all details of the work, verify dimensions in the field, and advise the Contracting Officer of any discrepancy before performing the work. 3.2 MANUFACTURER'S SERVICES Provide the services of the manufacturer's representative experienced in the installation, adjustment, and operation of the equipment specified, who will supervise the installing, adjusting, and commissioning and compliance testing of the equipment. 3.3 INSTALLATION Install equipment and material as indicated and in accordance with manufacturer's written instructions and NFPA 82 , with combustion air supply and ventilation in accordance with NFPA 31 or NFPA 54 as applicable. 3.3.1 Foundation a. Construct the incinerator foundation using [21] [_____] Mpa [3000] [_____] psi concrete as specified in Section 03 31 00.00 10 CAST-IN-PLACE STRUCTURAL CONCRETE. Extend the foundation a minimum of 1 m 3 feet beyond the incinerator on 3 sides and not less than 2.5 m 8 feet on the side where the ashes are removed. Install the incinerator in accordance with manufacturer's written instructions. b. Make proper provision for expansion and contraction between incinerator foundation and floor; pack the joint with suitable nonasbestos rope and fill with suitable compound that will not become soft at a temperature of 40 degrees C 100 degrees F. c. Provide incinerator supports which permit free expansion and contraction of each portion of the incinerator without placing undue stress on any part of the incinerator or setting. Set anchor bolts accurately, and of adequate length to install the incinerator. When embedded in concrete, provide anchor bolts with plates welded on the head and protect against damage until the equipment is installed. 3.3.2 Stack Support NOTE: Indicate design wind force that the stack will have to withstand. Also include in structural design seismic resistance, and coordinate with subparagraph Lateral Loads under paragraph SYSTEM DESCRIPTION. Provide stack support in accordance with NFPA 82 and NFPA 211, as applicable. Provide vertical and lateral supports for exterior chimneys to withstand wind forces of [_____] km/hour mph. 3.4 FIELD PAINTING Perform painting required for surfaces not otherwise specified, and finish painting of items only primed at the factory, as specified in Section 09 90 00 PAINTS AND COATINGS. 3.5 FIELD TRAINING NOTE: Consult equipment manufacturer for recommended time required to train personnel for the proper operation of the unit, and insert number of hours. a. Submit [Six] [_____] complete copies of operating instructions outlining the step-by-step procedures required for system startup, operation and shutdown. Include in instructions the manufacturer's name, model number, service manual, parts list, and brief description of all equipment and their basic operating features. And [Six] [_____] complete copies of maintenance instructions listing routine maintenance procedures, possible breakdowns and repairs, troubleshooting guides, and simplified schematic diagrams for the system as installed. b. Submit Incinerator _{Data Package 4} in accordance with Section 01 78 23 OPERATION AND MAINTENANCE DATA. c. Conduct a training course for the operating staff, as designated by the Contracting Officer, consisting of a total [_____] hours of normal working time, and starting after the system is functionally completed but prior to final acceptance tests. Cover in field instructions all of the items contained in the _{operating and maintenance instructions}, as well as demonstrations of routine maintenance operations. Notify the Contracting Officer at least 14 days prior to starting date of the training course. 3.6 _{ADJUSTING AND TESTING} 3.6.1 Performance Test a. Upon completion of all related work and prior to acceptance, subject the incinerator and associated equipment and instrumentation to the tests required to demonstrate specified performance. Notify the Contracting Officer [_____] days prior to conducting the test. b. Furnish all instruments and personnel required for the tests, including all equipment, apparatus, and materials, except waste materials, used for testing. The Government will supply [fuel,] [water,] [electric power,] [and] waste materials. Make two instruction manuals available at all times during the tests. The Contracting Officer's presence is required at all tests. c. Submit certified test reports in booklet form showing field tests performed to adjust each component, and all field tests performed to prove compliance with the specified performance criteria, upon completion and testing of the installed system. Indicate the final position of controls in each test report. 3.6.2 Fuel Systems Provide fuel system tests in accordance with Section 33 56 10 FACTORY-FABRICATED FUEL STORAGE TANKS. 3.6.3 _Performance Preheat the incinerator for [4] [_____] hours to reach the firing temperature of [982] [_____] degrees C [1800] [_____] degrees F. Weigh and record the total charge weight. Charge the incinerator at the rated burning capacity in kg pounds per hour for a period of [4] [_____] hours and operate in accordance with the manufacturer's written instructions. Include in performance testing the operation of the mechanical charging facilities, the incinerator, [the heat recovery boiler,] the air pollution control equipment, the ash handling equipment, and the operation monitoring facilities. Perform testing full scale for a full-operation cycle, and monitor performance to verify compliance with the contract requirements; submit a report on monitoring results. Reduce the waste to a fine ash residue. Follow normal burnout procedure. After the incinerator has cooled, weigh the residue. The weight of the residue sall not exceed [5.0] [_____] percent combustible material of the total charge weight. After clean-out, the incinerator shall not show any evidence of deterioration, such as slagged or spalling refractory, warping of parts, and discolored exterior paint. 3.6.4 Control Test the incinerator under actual firing conditions. Verify with testing that all controls function within the maximum and minimum limits for temperature or timing. Simulate actual unsafe conditions such as high temperatures and flame failure by reducing the settings for the activation of limit and safety controls. 3.6.5 Shell Temperature Operate the incinerator under normal load conditions for not less than [4] [_____] hours. After [4] [_____] hours, temperature readings of the outer shell, taken at not less than 5 random locations, shall not exceed the temperature limitation of paragraph FURNACE CONSTRUCTION.