1、*USACE / NAVFAC / AFCESA / NASA UFGS-02 53 16 (February 2010)-Preparing Activity: USACE SupersedingUFGS-02 53 16 (October 2007)UNIFIED FACILITIES GUIDE SPECIFICATIONSReferences are in agreement with UMRL dated April 2010*SECTION TABLE OF CONTENTSDIVISION 02 - EXISTING CONDITIONSSECTION 02 53 16REMED
2、IATION OF CONTAMINATED SOILS BY THERMAL DESORPTION02/10PART 1 GENERAL1.1 UNIT PRICE1.2 REFERENCES1.3 SYSTEM DESCRIPTION1.3.1 Design Requirements1.3.1.1 Primary Desorption Chamber1.3.1.2 Air Pollution Control System Requirements1.3.2 Performance Requirements1.3.2.1 Treatment Criteria1.3.2.2 Emission
3、Criteria1.3.2.3 Slagging Control1.4 SITE SPECIFIC TREATABILITY STUDIES1.5 SEQUENCING AND SCHEDULING1.6 INSTRUMENTATION AND CONTROLS1.6.1 Control Room1.6.2 Redundancies1.6.3 Displays and Data1.6.4 Stack Emissions Monitoring and Sampling1.6.5 Sampling1.6.6 Interlocks and Alarms1.6.6.1 Visible Alarms1.
4、6.6.2 Audible Alarms1.6.6.3 Remote Alarms1.6.7 Electrical Work1.7 CONTAMINATED MATERIAL FEED SYSTEM1.7.1 Support Equipment1.7.2 Capacity1.7.3 Metering1.7.4 Rehydration1.8 AIR SUPPLY AND POLLUTION CONTROL SYSTEMS1.8.1 Air Supply1.8.2 Induced Draft (ID) Fan1.8.3 Fugitive Emissions Control1.8.4 Quench1
5、.8.5 Stack Emissions ControlSECTION 02 53 16 Page 1Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-1.8.6 Water and Liquid Waste1.9 PROCESS RESIDUALS1.9.1 Liquid Wastes1.9.2 Solids1.10 AUXILIARY FUEL SYSTEM1.10.1 Feed Capability1.10.2 Secondary Contai
6、nment1.11 SUBMITTAL REQUIREMENTS1.12 SUBMITTALS1.13 QUALITY ASSURANCE1.13.1 Ambient Air Emissions and Noise Control1.13.2 Hazardous Materials1.13.3 Proof of Performance1.13.4 Installation1.13.5 Detail Drawings1.14 SITE CONDITIONSPART 2 PRODUCTS2.1 EQUIPMENT, MATERIALS AND STORAGE2.1.1 Capacity2.1.2
7、Segregation of Materials2.1.3 Instrumentation, Sensors, Recorders, and Sampling2.2 ConveyorsPART 3 EXECUTION3.1 LAYOUT3.1.1 Equipment3.1.2 Stockpiles3.1.3 Fuel System3.2 INSTALLATION/ERECTION/REMOVAL3.3 SAMPLING, MONITORING AND INSPECTIONS3.3.1 Minimum Sampling3.3.2 Stack Sampling3.3.3 Visual Inspec
8、tions3.3.4 Interlocks, Automatic Cut-Offs and Alarms3.4 LOGS3.5 STARTUP3.5.1 Startup Plan3.5.2 Systems Demonstration3.5.3 Instrumentation Calibration3.5.4 Control Interlock Demonstration3.5.5 24 Hour Operation3.5.6 Reporting3.6 PROOF OF PERFORMANCE PLAN3.6.1 Schedule3.6.2 Source of Material3.6.3 Ope
9、rating Conditions3.6.4 Field Proof of Performance Report3.6.4.1 Quantitative Analysis of the Materials3.6.4.2 Quantitative Analysis of the Stack Gases3.6.4.3 Material and Energy Balances3.6.4.4 Fugitive Emissions3.6.4.5 Continuous Measurement and Recording3.6.4.6 Other Requirements3.7 UTILITIES3.7.1
10、 Electricity3.7.2 WaterSECTION 02 53 16 Page 2Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-3.7.3 Natural Gas3.8 DEMOBILIZATION PLAN- End of Section Table of Contents -SECTION 02 53 16 Page 3Provided by IHSNot for ResaleNo reproduction or networkin
11、g permitted without license from IHS-,-,-*USACE / NAVFAC / AFCESA / NASA UFGS-02 53 16 (February 2010)-Preparing Activity: USACE SupersedingUFGS-02 53 16 (October 2007)UNIFIED FACILITIES GUIDE SPECIFICATIONSReferences are in agreement with UMRL dated April 2010*SECTION 02 53 16REMEDIATION OF CONTAMI
12、NATED SOILS BY THERMAL DESORPTION02/10*NOTE: This guide specification covers the requirements for onsite thermal desorption of non-radioactive materials contaminated by hazardous or toxic organic wastes and by petroleum, oil, or lubricants (POL).Edit this guide specification for project specific req
13、uirements 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 welc
14、ome 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).*PART 1 GENERAL1.1 UNI
15、T PRICE*NOTE: The unit price for thermal desorption should be based on in-situ volume. For liquids and sludges the unit of measure should be mass. Materials requiring retreatment should be segregated from treated materials.*The amount of material to be treated shall be verified by in-place measureme
16、nt mass. The quantity of materials requiring retreatment shall be reported and subtracted from the daily production when calculating SECTION 02 53 16 Page 4Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-treatment costs.1.2 REFERENCES*NOTE: This para
17、graph 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 Wizards Check Reference feature when you add a RID
18、outside of the Sections Reference Article to automatically place the reference in the Reference Article. Also use the Reference Wizards 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
19、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.AMERICAN WELDING SOCIETY (AWS)AWS B2.1/B2.1M (2009) Specification
20、for Welding Procedure and Performance QualificationAWS D1.1/D1.1M (2008; Errata 2008) Structural Welding Code - SteelASME INTERNATIONAL (ASME)ASME B40.100 (2005) Pressure Gauges and Gauge AttachmentsASME BPVC SEC IX (2007; Addenda 2008; Addenda 2009) Boiler and Pressure Vessel Code; Section IX, Weld
21、ing and Brazing QualificationsASME PTC 19.3 (1974; R 2004) Temperature MeasurementASTM INTERNATIONAL (ASTM)ASTM E 122 (2009) Calculating Sample Size to Estimate, With a Specified Tolerable Error, the Average for Characteristic of a Lot or ProcessASTM E 953/E 953M (2008) Fusibility of Refuse-Derived
22、Fuel (RDF) AshSECTION 02 53 16 Page 5Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-ISA - INTERNATIONAL SOCIETY OF AUTOMATION (ISA)ISA MC96.1 (1982) Temperature Measurement ThermocouplesNATIONAL FIRE PROTECTION ASSOCIATION (NFPA)NFPA 211 (2010) Stan
23、dard for Chimneys, Fireplaces, Vents, and Solid Fuel-Burning AppliancesNFPA 30 (2008; Errata 08-1) Flammable and Combustible Liquids CodeNFPA 31 (2006; Errata 06-1 Am 08-1; Am 08-2; Am 08-3; Amt 08-4) Liquefied Petroleum Gas CodeNFPA 70 (2008; AMD 1 2008) National Electrical CodeNFPA 82 (2009) Stand
24、ard on Incinerators and Waste and Linen Handling Systems and EquipmentNATIONAL INSTITUTE OF STANDARDS AND TECHNOLOGY (NIST)NIST SP 250 (1991) Calibration Services Users GuideU.S. ENVIRONMENTAL PROTECTION AGENCY (EPA)EPA 450/4-80/023R (1985) Guideline for Determination of Good Engineering Practice St
25、ack Height (Technical Support Document for the Stack Height Regulations)U.S. NATIONAL ARCHIVES AND RECORDS ADMINISTRATION (NARA)40 CFR 264 Standards for Owners and Operators of Hazardous Waste Treatment, Storage, and Disposal Facilities1.3 SYSTEM DESCRIPTIONThe thermal desorption system shall be pro
26、vided and operated by the Contractor to transfer organic compounds from contaminated materials to a gaseous stream drawn through the system. The system shall consist of a process or series of processes designed to remove organic contaminants from the contaminated materials by heating the soil or slu
27、dge matrix. Removal/treatment of organic vapors shall be completed in one or more air pollution control systems.1.3.1 Design Requirements*NOTE: The first option is preferred. It is more difficult to enforce schedule constraints with the second option.SECTION 02 53 16 Page 6Provided by IHSNot for Res
28、aleNo reproduction or networking permitted without license from IHS-,-,-*The capacity of the system shall be consistent with the remedial action schedule a minimum of _ kg/hour tons/hour. Modifications to the system shall be the Contractors responsibility; however, no modifications shall be performe
29、d without the Contracting Officers approval.1.3.1.1 Primary Desorption Chamber*NOTE: This paragraph is applicable to rotary kiln technology only. If batch processes are used, remove this paragraph.*The primary desorption chamber volatilizes the compounds of concern. The primary chamber shall be dire
30、ctly fired with the primary chamber operated at a pressure lower than atmospheric. indirectly fired. An inert carrier gas shall be recycled through the desorber and stack emissions treatment system.1.3.1.2 Air Pollution Control System Requirements*NOTE: If site materials contain PCBs, consider elimi
31、nating the use of an afterburner to alleviate permitting problems during construction.*The air pollution control system shall contain an afterburner. The temperature of the afterburner shall be greater than the temperature of the primary chamber a quench followed by an adsorption type treatment syst
32、em a condenser followed by an adsorption type treatment system _.1.3.2 Performance Requirements1.3.2.1 Treatment CriteriaMaximum contaminant concentrations allowed in thermally treated materials shall be as follows:ORGANIC CONTAMINANT TREATMENT CRITERIA(mg/kg)Trichloroethylene 10_ _Materials that do
33、 not meet the treatment criteria shall be retreated until the treatment criteria are met.1.3.2.2 Emission Criteria*NOTE: Current federal regulations are not directly applicable to thermal desorption. The designer should perform an air pathway analysis per ETL 1110-1-174 and obtain the State or air q
34、uality regional requirements. Include mass or concentration limits, as appropriate.SECTION 02 53 16 Page 7Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-*The system shall be designed to prevent exceeding ambient air quality standards as established
35、by the State, and to minimize health risks associated with thermal desorption system emissions, as shown in TABLE 1.TABLE 1EXHAUST GAS CRITERIACOMPONENT FEDERAL STATE-organic removal efficiency (minimum %) _ _-total hydrocarbons _ _-O2 (minimum) _ _-CO _ _-HCl _ _-metals _ _-particulates _ _-1.3.2.3
36、 Slagging Control*NOTE: The treatability study should determine the ash fusion temperature of the feed materials in accordance with ASTM E 953/E 953M.*Slagging shall be minimized by operating at _ degrees C degrees F less than the ash fusion temperature of the feed materials, as determined by ASTM E
37、 953/E 953M.1.4 SITE SPECIFIC TREATABILITY STUDIES*NOTE: Coordinate list of applicable treatability studies. Treatability studies performed on the site materials should be documented in this paragraph or furnished as an attachment to this section of the specifications. Summarize the results in this
38、paragraph.*_1.5 SEQUENCING AND SCHEDULING*NOTE: Verify that objectives have been identified in PART 3.*SECTION 02 53 16 Page 8Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-Documentation of successful accomplishment of the objectives of each phase o
39、f operation is required prior to approval to begin the next phase of operations. Mobilization shall include transportation of the equipment to the site, equipment erection and installation, but not operation. Mobilization shall not commence until approval of the mobilization plan is received from the Contracting Officer.1.6 INSTRUMENTATION AND CONTROLSContinuous emission monitors shall be in accordance with the appropriate Performance Specifications and EPA 450/4-80/023R. Systems shall be adequately protected from damage from onsite activity.1.6.1 Control Ro
