ARMY UFGS-02 53 13-2010 REMEDIATION OF CONTAMINATED SOILS AND SLUDGES BY INCINERATION《通过焚化修复受污染的土壤和淤泥》.pdf

《ARMY UFGS-02 53 13-2010 REMEDIATION OF CONTAMINATED SOILS AND SLUDGES BY INCINERATION《通过焚化修复受污染的土壤和淤泥》.pdf》由会员分享，可在线阅读，更多相关《ARMY UFGS-02 53 13-2010 REMEDIATION OF CONTAMINATED SOILS AND SLUDGES BY INCINERATION《通过焚化修复受污染的土壤和淤泥》.pdf（34页珍藏版）》请在麦多课文档分享上搜索。

1、*USACE / NAVFAC / AFCESA / NASA UFGS-02 53 13 (May 2010)-Preparing Activity: USACE SupersedingUFGS-02 53 13 (April 2006)UNIFIED FACILITIES GUIDE SPECIFICATIONSReferences are in agreement with UMRL dated April 2010*SECTION TABLE OF CONTENTSDIVISION 02 - EXISTING CONDITIONSSECTION 02 53 13REMEDIATION

2、OF CONTAMINATED SOILS AND SLUDGES BY INCINERATION05/10PART 1 GENERAL1.1 MEASUREMENT AND PAYMENT1.1.1 Metering1.1.2 Utilities1.2 REFERENCES1.3 SYSTEM DESCRIPTION1.3.1 Design Requirements1.3.2 Performance Requirements1.3.3 Site Specific Treatability Studies1.3.4 Auxiliary Fuel System1.3.4.1 Capacity1.

3、3.4.2 Feed Capability1.3.4.3 Secondary Containment1.4 SEQUENCING AND SCHEDULING1.4.1 Mobilization1.4.2 Startup Operations1.4.3 Trial Burn and Interim Operations1.4.4 Production Operations1.4.5 Demobilization1.5 SUBMITTALS REQUIREMENTS1.6 SUBMITTALS1.7 QUALITY ASSURANCE1.7.1 Emission Criteria1.7.2 Sl

4、agging Control1.7.3 Air Supply and Pollution Control systems1.7.3.1 Combustion Air1.7.3.2 Induced Draft Fan1.7.3.3 Fugitive Emissions Control1.7.3.4 Quench1.7.3.5 Stack Emissions Control1.7.3.6 Water and Liquid Waste1.7.4 Process Residuals1.7.4.1 Liquid Wastes1.7.4.2 Solids1.8 ENVIRONMENTAL REQUIREM

5、ENTSSECTION 02 53 13 Page 1Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-1.8.1 Existing Conditions1.8.2 ErectionPART 2 PRODUCTS2.1 MATERIALS AND EQUIPMENT2.1.1 Source of Material2.1.2 Equipment2.1.3 Instrumentation and Controls2.1.4 Control Room2.1

6、.5 Redundancies and Safety Procedures2.1.6 Data2.1.6.1 Copies2.1.6.2 Software Packages2.1.7 Instrumentation, Sensors, Recorders, and Sampling2.1.7.1 Instrumentation2.1.7.2 Stack Emissions Monitoring2.1.7.3 Stack Sampling2.2 ALARM EQUIPMENT2.2.1 Interlocks and Alarms2.2.1.1 Interlocks2.2.1.2 Visible

7、Alarms2.2.1.3 Audible Alarms2.2.1.4 Remote Alarms2.3 CONTAMINATED MATERIAL FEED SYSTEM2.3.1 Support Equipment2.3.2 Capacity2.3.3 Metering2.3.4 Conveyors2.4 TREATED MATERIAL AND ASH SYSTEMS2.4.1 Capacity2.4.2 Segregation of Materials2.4.3 RehydrationPART 3 EXECUTION3.1 LAYOUT3.1.1 Excavation and Stoc

8、kpiling3.1.2 Fuel System3.2 INSTALLATION/ERECTION/REMOVAL3.3 SAMPLING, MONITORING AND INSPECTIONS3.3.1 Additional Sampling3.3.2 Minimum Sampling Frequency3.3.2.1 Contaminated Material3.3.2.2 Treated Material3.3.2.3 Fly Ash3.3.3 Contaminated Material Sampling3.3.4 Treated Material and Fly Ash Samplin

9、g3.3.5 Stack Sampling3.3.6 Monitoring3.3.7 Visual Inspections3.3.8 Interlocks, Automatic Cut-Offs and Alarms3.4 DATA3.5 STARTUP OPERATIONS3.6 UNCONTAMINATED MATERIAL OPERATION3.6.1 Material Handling Demonstration3.6.2 Instrumentation Calibration3.6.3 Control Interlock Demonstration3.6.4 Hot CheckSEC

10、TION 02 53 13 Page 2Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-3.6.5 24-Hour Continuous Operation3.7 CONTAMINATED MATERIAL OPERATION3.7.1 Shakedown3.7.2 72 Consecutive Hours of Operation3.7.3 Reporting3.8 MINI-BURN3.8.1 Operating Conditions3.8.2

11、 Reporting3.9 PRETRIAL BURN3.9.1 Pretrial Burn Results3.9.2 Pretrial Burn Operations3.9.3 Initial Trial Burn Attempt3.9.4 Time Extension3.10 TRIAL BURN3.10.1 Schedule3.10.2 Operating Conditions3.10.3 Trial Burn Report3.10.3.1 Quantitative Analysis of the Materials3.10.3.2 Quantitative Analysis of th

12、e Stack Gases3.10.3.3 Material and Energy Balances3.10.3.4 Fugitive Emissions3.10.3.5 Continuous Measurement and Recording3.10.3.6 Other Requirements3.11 TRIAL BURN APPROVAL3.11.1 Failure3.11.2 Second and Third Trial Burns3.11.3 Successful Trial Burns3.11.4 Default3.11.5 Multiple Incineration Units3

13、.12 INTERIM OPERATIONS3.12.1 Mass Feed Rate3.12.2 Primary Chamber3.12.3 Secondary Combustion Chamber3.12.4 Air Pollution Control System3.12.5 Sampling and Analysis3.13 PRODUCTION OPERATIONS3.13.1 Schedule3.13.2 Requirements3.13.2.1 Startup and Shutdown3.13.2.2 Changes3.13.2.3 Performance3.14 DEMOBIL

14、IZATION- End of Section Table of Contents -SECTION 02 53 13 Page 3Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-*USACE / NAVFAC / AFCESA / NASA UFGS-02 53 13 (May 2010)-Preparing Activity: USACE SupersedingUFGS-02 53 13 (April 2006)UNIFIED FACILITI

15、ES GUIDE SPECIFICATIONSReferences are in agreement with UMRL dated April 2010*SECTION 02 53 13REMEDIATION OF CONTAMINATED SOILS AND SLUDGES BY INCINERATION05/10*NOTE: This guide specification covers the requirements for onsite incineration of non-radioactive materials contaminated by hazardous or to

16、xic organic wastes.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

17、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 shou

18、ld be submitted as a Criteria Change Request (CCR).*PART 1 GENERAL*NOTE: This performance specification does not specify the capacity of the incinerator. The Contractor determines the capacity of a transportable incineration system (TIS) required to meet the schedule. The Contractor should be allowe

19、d to use an existing, proven incinerator that has a permit for similar wastes.Disposal of process residuals is not included in this section. Additional treatment of the treated material and/or the fly ash is frequently required to satisfy the toxicity characteristic leachate procedure (TCLP) for met

20、als.SECTION 02 53 13 Page 4Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-Management of project records is not included in this section. Refer to the appropriate section.*1.1 MEASUREMENT AND PAYMENT*NOTE: The unit price for incineration should be ba

21、sed on site surveys before and after excavation/removal for in-situ volume when soils are being treated. For liquids and sludges, the unit of measure should be weight or volume, depending on the characteristics of the material. Materials requiring retreatment shall be segregated from treated materia

22、ls.*The amount of material to be treated shall be verified by in-place measurement.1.1.1 Metering*NOTE: Payment should be based on surveyed in-situ volume because of the variation of moisture content of the soils or sludges. Include this paragraph when required for process control of the treatment s

23、ystem.*Provisions shall be made for weighing the daily production of treated material and fly ash with an accuracy of plus or minus 2 percent.1.1.2 Utilities*NOTE: The utilities requirements for the incineration system should be identified in the Contractors design. The following information could b

24、e used as a check: the amount required for a 12,000 - 18,000 kg (15 - 20 ton) per hour incinerator is 5 - 35 liters per second (75 - 600 gpm) of water, 1200 - 2500 kw of electricity and 30 - 60 cubic meters per minute (1000 - 2000 scfm) of natural gas. The Contractor should verify the adequacy of th

25、e existing utilities and be responsible for the required agreements with the utility companies for usage and any required changes.Points of connection are normally shown on the drawings. Occasionally names, addresses, and telephone numbers of the utility companies are shown on the drawings. Delete t

26、he following paragraphs if the information is shown elsewhere.*Provide fuel and utilities at locations shown on the drawings. Verify availability and locations of utilities and compensate the utility company SECTION 02 53 13 Page 5Provided by IHSNot for ResaleNo reproduction or networking permitted

27、without license from IHS-,-,-for connection and usage. Submit peak and average system requirements for electricity, water, waste water disposal, natural gas and other fuels.a. Electricity: The power utility company is _, phone number _.b. Water: The water utility company is _, phone number _.c. Natu

28、ral Gas: The natural gas utility company is _, phone number _.d. Sewer: The sewer utility company for disposal of domestic waste only domestic waste and treated wastewater is _, phone number _.1.2 REFERENCES*NOTE: This paragraph is used to list the publications cited in the text of the guide specifi

29、cation. 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 outside of the Sections Reference Article to automatically place the referenc

30、e 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 you choose to reconcile references in the publish print process.*The publicat

31、ions 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.ASTM INTERNATIONAL (ASTM)ASTM E 122 (2009) Calculating Sample Size to Estimate, With a Specified Tolerable Error, the Average for Characteristi

32、c of a Lot or ProcessASTM E 953/E 953M (2008) Fusibility of Refuse-Derived Fuel (RDF) AshNATIONAL FIRE PROTECTION ASSOCIATION (NFPA)NFPA 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 CodeNATIONAL I

33、NSTITUTE 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 Stack Height (Technical Support Document for the Stack Height Regulations)EPA 625/

34、6-89/019 (1989) Handbook: Guidance on Setting Permit Conditions and Reporting Trial Burn Results: Volume II of the Hazardous Waste Incineration Guidance SeriesEPA 625/6-89/021 (1989) Handbook Hazardous Waste Incineration Measurement Guidance Manual: Volume III of the Hazardous Waste Incineration Gui

35、dance SeriesEPA 625/6-89/023 (1990) Handbook: Quality Assurance/Quality Control (QA/QC) Procedures For Hazardous Waste IncinerationU.S. NATIONAL ARCHIVES AND RECORDS ADMINISTRATION (NARA)40 CFR 264 Standards for Owners and Operators of Hazardous Waste Treatment, Storage, and Disposal Facilities40 CF

36、R 266 Standards for the Management of Specific Hazardous Wastes and Specific Types of Hazardous Waste Management Facilities40 CFR 270 EPA Administered Permit Programs: The Hazardous Waste Permit Program40 CFR 60 Standards of Performance for New Stationary Sources40 CFR 61 National Emission Standards

37、 for Hazardous Air Pollutants40 CFR 761 Polychlorinated Biphenyls (PCBs) Manufacturing, Processing, Distribution in Commerce, and Use Prohibitions1.3 SYSTEM DESCRIPTIONProvide and operate a transportable incineration system (TIS) to transfer organic compounds from contaminated materials to an air st

38、ream for SECTION 02 53 13 Page 7Provided by IHSNot for ResaleNo reproduction or networking permitted without license from IHS-,-,-destruction. 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 s

39、ludge matrix. The incineration system shall consist of a combination of the following: feed system, primary chamber, secondary combustion chamber, cyclones, scrubbers, precipitators, quench chamber, fabric filters, treated material removal system, fly ash removal system, and ancillary equipment. The

40、 primary heating chamber volatilizes and may initiate combustion of organic compounds. Oxidation of organic vapors to carbon dioxide and water shall be completed in the secondary combustion chamber, or afterburner, at the specified temperature, which is greater than the temperature of the primary ch

41、amber. Systems that do not destroy the organic contaminants are not acceptable.1.3.1 Design RequirementsDesign the incineration system in accordance with 40 CFR 264 Section .343. When CFR requirements conflict with those specified, the more stringent requirement shall apply unless otherwise approved

42、. Proposed systems that differ from the specified system shall have well documented equivalent or better operational and performance capabilities. Modifications to the system required to treat the contaminated materials onsite shall be the Contractors responsibility.1.3.2 Performance Requirements*NO

43、TE: List the contaminants that will be used to determine the effectiveness of the incineration process and the cleanup criteria applicable to each.*Maximum contaminant concentrations allowed in thermally treated materials shall be as follows:ORGANIC CONTAMINANT TREATMENT CRITERIA (mg/kg)_ _1.3.3 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 at