Technical Basis for Proposed ASME Code Case for Construction of Compact Heat Exchangers in High Temperature Reactors

2021 ◽  
Author(s):  
Robert Keating ◽  
Suzanne McKillop

Abstract The U.S. Department of Energy has recently completed a research program to support the development of the compact heat exchanger (CHX) for use in high temperature advanced reactors. The project was executed by an Integrated Research Project (IRP) and includes team members from the University of Wisconsin–Madison, University of Michigan, Georgia Institute of Technology, University of Idaho, North Carolina State University, Oregon State University, Electric Power Research Institute, MPR Associates, and heat exchanger manufacturers CompRex and Vacuum Process Engineering. The research was guided by a roadmap to support the eventual adoption of an American Society of Mechanical Engineers (ASME) Boiler and Pressure Vessel Code, Section III, Code Case for compact heat exchanger designs in high temperature reactor service. This roadmap is outlined in Journal of Nuclear Engineering and Radiation Science, NERS 19-1161, which identified specific research gaps to support the Code Case. The IRP has completed the research and the ASME Section III Standards Committee is in the process of writing and approving a Code Case for Section III, Division 5, Class A applications. This paper provides the detailed technical basis for the ASME Code Case for CHX. The paper provides a vital link between the research results and the proposed Code Case and closes the research gaps that are tied to the original Roadmap. In addition, the paper provides further detailed commentary on the proposed requirements. The major technology gaps included material properties, failure modes and effects, analysis methods, and examination methods. The IRP studied basic material properties of diffusion bonded plate, creep and fatigue models, development of NDE methodology and development of advanced analytical approaches to design.

Energy ◽  
2014 ◽  
Vol 75 ◽  
pp. 104-115 ◽  
Author(s):  
Wen-xiao Chu ◽  
Ting Ma ◽  
Min Zeng ◽  
Ting Qu ◽  
Liang-bi Wang ◽  
...  

Author(s):  
Merrill A. Wilson ◽  
Charles Lewinsohn ◽  
James Cutts ◽  
Valery Ponyavin

It has been proposed that compact ceramic heat exchangers can be used for high temperature, corrosive applications. This paper discusses the design development of a micro-channel heat exchanger for the decomposition of sulfuric acid as part of the hydrogen producing sulfur iodine thermo-chemical cycle. Corrosion studies of candidate materials indicate that ceramic materials have superior corrosion and creep resistance under these high temperature, high acid concentration environments. This compact heat exchanger utilizes micro-channels to enhance the heat transfer while maintaining low pressure drops within the system. Through modular stacking of these micro-channel networks, a "shell and plate" configuration enables the processing of commercial-scale processes. The ceramic materials provide for long-life applications. The design of the micro-channel features captures the enhanced heat transfer characteristics at the micro-scale; the modular assembly permits the integration into macro-scale processes. As a case study, the thermal performance and the economics were investigated to determine the feasibility of this compact heat exchanger for the hydrogen producing sulfur iodine thermo-chemical cycle. The results of this design effort with its associated performance goals and development status will be reported.


2019 ◽  
Vol 154 ◽  
pp. 208-216 ◽  
Author(s):  
Jojomon Joseph ◽  
Michel Delanaye ◽  
Rabia Nacereddine ◽  
Andres Giraldo ◽  
Mehdi Rouabah ◽  
...  

Author(s):  
G. K. Housley ◽  
J. E. O’Brien ◽  
G. L. Hawkes

Design details of a compact heat exchanger and supporting hardware for heat recuperation in a high-temperature electrolysis application are presented. The recuperative heat exchanger uses a vacuum-brazed plate-fin design and operates between 300 and 800°C. It includes corrugated inserts for enhancement of heat transfer coefficients and extended heat transfer surface area. Two recuperative heat exchangers are required per each four-stack electrolysis module. The heat exchangers are mated to a base manifold unit that distributes the inlet and outlet flows to and from the four electrolysis stacks. Results of heat exchanger design calculations and assembly details are also presented.


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