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Report to
Congress Treatment & Immobilization of Hanford Radioactive Tank Waste |
4.0 The Decision to Proceed
DOEs review of the contractor deliverables for Part A led to the following decisions.
This section summarizes the distinct decisions that support DOEs authorization to proceed with Part B of the TWRS Phase I project. First, the contractors January 1998 proposals are summarized along with the changes in the original 1996 contracts that were proposed and selected for further evaluation. Next, the evaluation and selection of the BNFL proposal is described. Then, the decision to include HLW services as well as LAW services is addressed. The details of the final negotiated agreement with BNFL are provided in Section 5.
To ensure that the path forward for treatment and immobilization of tank waste was the best possible, DOE developed and implemented a systematic decision process to evaluate contractor deliverables. (See Appendix A for a detailed description of the decision process.) This process focused on the three criteria defined in the original RFP:
In addition, the decision process included a determination of the readiness-to-proceed of key supporting organizations (i.e., DOE-RL, the TWRS DOE Regulatory Unit, and the Hanford M&I Contractor) and whether the impact of the contractor approaches remained bounded by the TWRS EIS under the National Environmental Policy Act. Review teams, including numerous experts from private industry, academia, national laboratories, and DOE contractors, also reviewed the basis for the decision and the decision itself (see Appendix B). Individuals with specific expertise in nuclear waste management, nuclear engineering, nuclear safety, project finance, cost estimating, complex construction management, privatization contracting, glass and vitrification technology, chemical and process engineering, radiochemical process design, decision modeling, economics and public policy, and systems management were included on the review teams. These reviews examined the decision at multiple levels of detail (e.g., from overall decision to specific details of readiness-to-proceed assessments and specific financial modeling).
4.1 Description of Contractor Approaches
The following sections describe the contractors proposals contained in their January 1998 Part A deliverables. In preparing the Part A submittals, the contractors were encouraged to propose enhancements to the contract that they believed would provide a better overall value to the government. BNFL proposed a series of enhancements as an alternate proposal, as described below in Section 4.1.2. LMAES did not propose technical enhancements to the contract. Instead, LMAES proposed an "alternative pricing approach" that would use a cost-reimbursement contract for much of the proposed work.
4.1.1 LMAES Approach
LMAES proposed an approach with several innovative, but untested technologies. Those technologies and their previous applications are shown in Table 4-1. The LMAES technical approach proposed to use a liquid-fed, high-temperature, ceramic melter for LAW immobilization; cold crucible melter for HLW immobilization; and ion-exchange, ozonation, and electrochemical processing for radionuclide removal. LMAES also proposed use of a contact maintenance approach for its LAW vitrification process. Contact maintenance can reduce facility costs (because of reduced shielding requirements), but would require additional separation processes to limit radiation exposure to workers. The additional separation processes proposed by LMAES were generally unproven for application with Hanford waste.
The LMAES business approach included numerous companies providing basic services to a Limited Liability Corporation. No member, including the Project Manager, LMAES, would have a controlling vote. The Project Manager would not be liable for the actions of first-tier subcontractors. The Limited Liability Corporation would have an executive management council comprised of Lockheed Martin Corporation (chair), Fluor Daniel Inc., COGEMA, and AEA Technology. LMAES proposed to provide the project management and systems integration elements as a subcontractor to the Limited Liability Corporation.
LMAES divided the work into 13 job lots and proposed to conduct work on a fixed-price basis for only three of those job lots. The remaining work would be performed on a cost-reimbursement basis. For example, under the LMAES proposal, fixed-unit prices for treated waste would not be set until at least one year after the hot start of the facility. LMAES proposed to recover project costs for design, construction, and startup whether or not their facility successfully processed waste.
BNFL proposed mature technologies for treatment and vitrification of the wastes, including use of a liquid-fed, low-temperature, ceramic melter based on the same technology used for HLW vitrification at the West Valley Demonstration Project in New York and the Defense Waste Processing Facility at the Savannah River Site in South Carolina. The proposed pretreatment technologies, including ion exchange, precipitation, and isotopic dilution, also have been applied at other facilities in the United Kingdom, Belgium, France, and Japan. Table 4-1 shows BNFLS proposed technologies for key treatment functions and their previous applications.
The BNFL team, as described in its Part A deliverables, is composed of BNFL Inc., BNFL Engineering Ltd., Bechtel National Inc. (Bechtel), GTS Duratek, and Science Applications International Corporation (SAIC). BNFL will be the prime contractor and majority owner of the special purpose corporation proposed for Part B. In addition, BNFL will be responsible for project management and integration, regulatory and nuclear safety management, and operations management.
BNFL submitted a proposal incorporating fixed-unit prices and also prepared a series of enhancements as an alternate proposal. The separate elements of BNFLs alternate proposal along with a summary of their merits are described below.
BNFL estimates that those capacity expansions would cost an additional $800 million in construction funds (in FY1997 values) and start expansion of the facility around 2011 to be completed in time for extended processing. If implemented, BNFL contends the expanded facility could enable immobilizing the waste in the 85 highest risk tanks by 2028. The waste in those tanks would account for 55% to 65% (by mass) of the total tank waste and approximately 95% of the long-lived radionuclides that would be mobile in the soil in case of a leak.
| Table 4-1. Major Applications of Treatment Technology Proposed by BNFL and LMAES | ||||
| Treatment Function | BNFL | LMAES | ||
| Technology Proposed | Application History | Technology Proposed | Application History | |
| LAW Concentration | Evaporation | Evaporation of alkaline supernatant at Hanford since the 1950s and at Savannah River since the 1960s | No Evaporation Proposed | Not applicable |
| Solid/Liquid Separation | Ultrafiltration/ Cross-Flow Filtration | Ultrafiltration/cross-flow filtration used at Enhanced Actinide Removal Plant at Sellefield, United Kingdom | Centrifuge, High Shear Rotary Filter | Centrifuges used for gross separation at
Hanfords
AR Vault facility and in France for uranium processing No known applications of high shear rotary filter used in nuclear production industry |
| Cesium Removal | Elutable Ion Exchange SL-644 | Elutable ion exchange used at Hanfords
B Plant in 1970s
Non-elutable ion exchange used at Hanfords B Plant in the 1970s and West Valley in the 1980-90s on chemically similar wastes |
Elutable Ion Exchange
Electro-Ion Exchange Membrane Ion Exchange |
Elutable ion exchangers used in nuclear
waste processing
Electro-ion exchange in initial development stage for cesium removal No known applications of membrane ion exchange used in nuclear waste processing |
| Strontium/ Transuranic Removal | Strontium-Nitrate Isotopic Dilution | Used in Hanfords B Plant to enhance recovery of strontium-90 from retrieved Hanford tank wastes | Ozonation | Ozonation tested on radioactive laboratory-scale at Hanford for organic de-complexation, but inefficient |
| Iron-Nitrate Precipitation (Ferric Floc Precipitation) | Used at Enhanced Actinide Removal Plant for transuranic recovery from liquid wastes. Similar physical process at Hanford and Savannah River for the settling of transuranic in alkaline Plutonium-Uranium Extraction Facility wastes | High Shear Rotary Filter | No known applications of high shear rotary filter used in nuclear production industry | |
| Technetium Removal | Elutable Ion Exchange SL-639 | 30,000 gallons of Hanford tank waste treated in 1960. Continued research on use of anion exchange to recover technetium from Hanford wastes | Electro-Reduction for Technetium Recovery
Electrodialysis for technetium purification |
Technology tested on radioactive laboratory-scale onlyresults unclear |
| Treatment Function | Technology Proposed | Application History | Technology Proposed | Application History |
| Cobalt and Europium Removal | Not Needed | Not applicable | Not Identified | Limited studies for wastes similar to tank wastes, but unknown if relevant to LMAES technology |
| LAW Vitrification | Liquid-Fed Ceramic MelterLow Temperature, 1,100 to 1,200 ° C | Technology used for HLW vitrification at
West Valley Demonstration Project and Defense Waste Processing Facility.
Also demonstrated at Pamela Facility in Mol, Belgium; Radioactive
Liquid-Fed Ceramic Melter at Hanford; and a demonstration melter in
Tokai Reprocessing Plant, Japan
Some LAW processing has been completed by Duratek at Savannah River, M-Area |
Liquid-Fed Ceramic MelterHigh Temperature, 1,250 to 1,350 ° C | Transportable vitrification system with small-scale melter incorporating some design features of proposed melter has been tested at Oak Ridge National Laboratory. Some innovative features are undemonstrated |
| LAW Maintenance Approach | Remote Operations Using Manipulators | Used at West Valley Demonstration Project, Defense Waste Processing Facility, United Kingdom, and France | Contact Maintenance | Not used in radioactive applications with highly volatile processes |
| HLW Concentration | Cross-Flow Filter for Supernatant Separation | Cross-flow filtration used at Enhanced Actinide Removal Plant at Sellefield, United Kingdom | Centrifuge | Centrifuges used for gross separation at Hanfords AR Vault facility and in France for uranium processing |
| Feed Preparation | Blending/ Evaporation | Process similar to that used in the West Valley and Defense Waste Processing Facility Projects for feed concentration | Acidification/ Blending | AVH Calciner used in the French R-7 and T-7 vitrification plants, with acidified feeds; some simulation work on Hanford-type wastes |
| HLW Vitrification | Liquid-Fed Ceramic Melter | Technology used for HLW vitrification at West Valley Demonstration Project and the Defense Waste Processing Facility. Also demonstrated at Pamela Facility in Mol, Belgium; Radioactive Liquid-Fed Ceramic Melter at Hanford; and a demonstration melter in Tokai Reprocessing Plant, Japan | Cold Crucible Melter | 70% scale melter tests performed with simulated HLW. Small-scale cold crucible melter used in LAW vitrification in Russia |
BNFLs alternate proposal was evaluated to be superior to its base proposal. Based on the above results, all elements of BNFLs alternate proposal were accepted for comparison with other possible programmatic approaches and as a basis for negotiations.
4.2 Evaluation of the Contractors Approaches
To support its decision to proceed with Part B, DOE conducted a systematic review of all deliverables from Part A. The evaluation of those products led to an initial determination of the viability of each contractor to meet Part B requirements and identified issues to be addressed during negotiations. The review also identified areas of concern for both teams. Therefore, in considering the viability of the two contractors, consideration was given to the features of the proposed approaches that could be refined through negotiations.
The technical viability assessment considered whether proposed technologies are likely to work. The primary consideration in assessing technical viability was the demonstrated maturity of the technologies, process flowsheets, and facility designs. The findings from this review are summarized below.
LMAES was judged to not be viable because the technical approach had an unacceptably high technical risk in attaining the DOEs cleanup goals. The LMAES contract deliverables did not provide sufficient evidence that the contractor could, with a high degree of confidence, successfully treat Hanford tank waste using the proposed technical approach in a timely manner. The LMAES approach uses numerous technologies that are research and development in nature. The approach was judged by DOE (and a group of external experts who assisted DOE with its review of the proposed waste treatment technology of both contractors) to be too risky and require substantial, additional development work. In DOEs judgment, the LMAES facility configuration and technical approach would likely undergo substantial change prior to the time that a waste treatment facility would be operational.
This determination by DOE was subjected to two outside reviews: one chartered by DOE-RL, and the second chartered by DOE Headquarters. (The review process and expertise of these reviewers are described in Appendix B.) Those reviews, while finding minor differences with the DOE determination, agreed on the central issue that the LMAES approach had an unacceptably high technical risk.
BNFL was judged viable because the technical approach was sound and the regulatory approach was reasonable. The business and financial terms were not acceptable as proposed and were addressed in subsequent negotiations. In general, the technologies chosen by BNFL for treatment and immobilization are mature, robust, and reliable and have resulted in a conservative process approach. In addition, the development requirements for the selected technologies were understood and identified, and a development program addressing those risks was clearly defined.
The independent review (see Appendix B) led to some refinements in the assessment of BNFL technologies and concurred with the determination that BNFL is viable for Part B. The independent review expressed some concern with the technology for technetium separation and suggested DOE should undertake a development program in parallel to that of BNFL.
DOE entered into negotiations with BNFL for both LAW and HLW treatment services. The Part A contracts provided for DOE to decide to contract for only LAW treatment services or for both LAW and HLW treatment services. DOE evaluated the alternative of including only LAW processing services during Phase I. This evaluation showed that proceeding with combined HLW and LAW processing services was preferred for several reasons.
The decision to proceed with BNFL satisfies the fundamental principles originally established for the contracting of privatized TWRS waste processing services.
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