scholarly journals A Study of Diffusion Bonding Process for High Temperature and High Pressure Micro Channel Heat Exchanger Using Inconel 617

Author(s):  
Chan Ho Song ◽  
Seok Ho Yoon ◽  
Joon Seok Choi
Author(s):  
Wenge Zhang ◽  
Xuedong Chen ◽  
Tiecheng Yang ◽  
Jianrong Li ◽  
Jilin Yu

Hydrogenation reactor vessel as a key heat exchanging element equipment endures both high pressure and high temperature. Its nozzle welding areas have complicated stress states with both high stress level and high stress grads (as well as high strain grads). Defects and cracks are frequently found just on the welds or at heat-influence area by ultrasonic non-destructive inspection for this kind of in-service heat exchanger. To acquire the accurate stress states of nozzle welding area are fundamental necessary step on safety assessment and residual life predication for the components as well as the heat exchanger. A three dimensional finite element analysis model is performed using the on-site parameters measured directly from the in-service equipment. The temperatures and stress distribution at the nozzle welding areas of hydrogenation reactor vessel are obtained. By applying the CVDA-84 standard codes to the area which contains initial defects, critical crack size can be calculated and the safety assessment can be performance.


Author(s):  
Byoung Ik Choi ◽  
Kui Soon Kim ◽  
Man Yeong Ha ◽  
Ji Hwan Jeong ◽  
Jong Rae Cho ◽  
...  

A computational study for the optimal design of heat exchangers used in a high temperature and high pressure system is presented. Two types of air to air heat exchangers are considered in this study. One is a single-pass cross-flow type with straight plain tubes and the other is a two-pass cross-counter flow type with plain U-tubes. These two types of heat exchangers have the staggered arrangement of tubes. The design models are formulated using the number of transfer units (ε-NTU method) and optimized using a genetic algorithm. In order to design compact light weight heat exchangers with the minimum pressure loss and the maximum heat exchange rate, the weight of heat exchanger core is chosen as the object function. Dimensions and tube pitch ratio of a heat exchanger are used as design variables. Demanded performance such as the pressure loss (ΔP) and the temperature drop (ΔP) are used as constraints. The performance of heat exchangers is discussed and their optimal designs are presented with an investigation of the effect of design variables and constraints.


Author(s):  
Merrill A. Wilson ◽  
Kurt Recknagle ◽  
Kriston Brooks

Typically, ceramic micro-channel devices are used for high temperature heat exchangers, catalytic reactors, electronics cooling, and processing of corrosive streams where the thermomechanical benefits of ceramic materials are desired. These benefits include: high temperature mechanical and corrosion properties and tailorable material properties such as thermal expansion, electrical conductivity and thermal conductivity. In addition, by utilizing Laminated Object Manufacturing (LOM) methods, inexpensive ceramic materials can be layered, featured and laminated in the green state and co-sintered to form monolithic structures amenable to mass production. In cooperation with the DOE and Pacific Northwest National Labs, silicon carbide (SiC) based micro-channel recuperator concepts are being developed and tested. The performance benefits of a high temperature, micro-channel heat exchanger are realized from the improved thermal efficiency of the high temperature cycles and the improved effectiveness of micro-channels for heat transfer. In designing these structures, the heat and mass transfer within the micro-channels are being analyzed with heat transfer models, computational fluid dynamics models and validated with experimental results. As an example, a typical micro-turbine cycle was modified and modeled to incorporate this ceramic recuperator and it was found that the overall thermal efficiency of the micro-turbine could be improved from about 27% to over 40%. Process improvements require technical advantages and cost advantages. These LOM methodologies have been based on well-proven industry standard processes where labor, throughput and capital estimates have been tested. Following these cost models and validation at the prototype scale, cost estimates were obtained. For the micro-turbine example, cost estimates indicate that the high-temperature SiC recuperator would cost about $200 per kWe. The development of these heat exchangers is multi-faceted and this paper focuses on the design optimization of a layered micro-channel heat exchanger, its performance testing, and fabrication development through LOM methodologies.


2003 ◽  
Author(s):  
Merrill A. Wilson ◽  
Steven M. Quist

Efficiency and emissions of advanced gas turbine power cycles can be improved by incorporating high-temperature ceramic heat exchangers (see Figure 1). In cooperation with the DOE, preliminary development and testing of SiC based structures has been completed. This program has focused on four initial areas: thermo-mechanical degradation as a function of the chemical operating environments, design of a layered microchannel heat exchanger, thermo-mechanical testing and analysis of these structures, and fabrication development through rapid prototyping techniques.


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