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A) Titanium B) Stainless steel C) Aluminum alloys D) Copper
A) Parallel flow B) Perpendicular flow C) Cross current flow D) Countercurrent flow
A) Reduce fluid velocity B) Minimize corrosion C) Increase surface area and create turbulent flow D) Decrease pressure drop
A) Welded type B) Soldered type C) Brazed type D) Gasket type to allow periodic disassembly, cleaning, and inspection
A) Low thermal efficiency B) Heavy weight C) High manufacturing cost D) Might cause clogging as the pathways are very narrow
A) Same weight as shell and tube heat exchangers B) Weight varies significantly with size C) Approximately 5 times lighter than shell and tube heat exchanger D) Heavier due to aluminum alloys
A) Low temperature services such as natural gas, helium and oxygen liquefaction plants B) Industrial boilers C) Hot water heating systems D) High pressure steam systems
A) Innovations in fluid dynamics B) Improvements in welding techniques C) Development of new alloys D) Advances in gasket and brazing technology
A) Enhance fluid flow rate B) Reduce manufacturing costs C) Increase heat transfer efficiency D) Create a reliable seal that prevents cross-contamination
A) Low to medium pressures B) High pressures C) Very low pressures D) Ultra-high pressures
A) Lower volume but higher cost B) Higher volume and cost C) Stacked-plate arrangement typically has lower volume and cost D) Same volume but higher cost
A) Soldered and glued plate varieties B) Bolted and riveted plate varieties C) Welded only D) Dip-brazed, vacuum-brazed, and welded plate varieties
A) High thermal conductivity B) Aluminum alloys are susceptible to Mercury Liquid Embrittlement Failure C) Resistance to corrosion D) Low cost
A) To enhance heat transfer and create turbulent flow B) To decrease weight C) To reduce manufacturing complexity D) To improve aesthetic appearance
A) High heat transfer efficiency B) Low cost C) Large size D) Ease of maintenance
A) Shell and tube only B) Only plate and frame C) Plate and frame, plate and shell, and spiral designs D) Spiral only
A) Decreases thermal efficiency B) Reduces pressure drop C) Increases manufacturing complexity D) Ensures fluid flows across the entire heat transfer surface, preventing stagnant zones
A) Counter-current configuration B) Perpendicular configuration C) Cross current configuration D) Parallel configuration
A) Requires no maintenance B) Automated cleaning systems C) Difficult to clean the pathways D) Easy to clean
A) Pressure handling varies greatly B) Able to withstand high pressure C) Cannot withstand high pressure D) Only suitable for low pressure
A) Direct contact flow. B) Parallel-flow, where fluids enter at the same end and travel parallel. C) Counter-flow, where fluids enter from opposite ends. D) Cross-flow, where fluids travel perpendicular to each other.
A) Colorimetric analysis. B) Thermodynamic performance testing (SAE J3094, etc.). C) Sound frequency measurement. D) Odor detection.
A) The Ramachandra K. Patil (et al.) method. B) The Charles E. Boardman method. C) The John H. Germer method. D) The Scott S. Haraburda method.
A) The Ramachandra K. Patil (et al.) method. B) The Charles E. Boardman method. C) The John H. Germer method. D) The Scott S. Haraburda method.
A) At an angle. B) Inverted. C) Vertically. D) Horizontally.
A) Oxygen production. B) Air filtration. C) Water desalination. D) Pasteurization.
A) Randomly placed welds. B) Circular patterns only. C) No welding is involved. D) A regular pattern of dots or a serpentine pattern of weld lines.
A) Pressurizing the enclosed space with sufficient force for direct-expansion of the thin metal. B) Cooling the metal rapidly after welding. C) Using thicker metal sheets. D) Applying adhesive between the layers.
A) A swelled pillow formed out of metal. B) Flat and smooth surfaces. C) Irregular, jagged shapes. D) Sharp edges and corners.
A) Marine industry B) Automotive industry C) Aerospace industry D) Food processing industry
A) Condenser B) Reboiler C) Steam generator D) Evaporator
A) Prandtl instability B) Reynolds instability C) Ledinegg instability D) Bernoulli instability
A) Compressor B) Expansion valve C) Evaporator D) Condenser
A) Moisture condensation on the air-side B) Expansion upon freezing C) Heat transfer rate D) Fouling prevention
A) Condensate B) Humidity C) Frost D) Evaporate
A) Use of refrigerants B) Indentations placed within the fins C) Thicker fin material D) Increased fin spacing
A) Pressure drops across the exchanger B) Heat exchange capacity (kW) C) Noise level during operation D) Thermal performance
A) Double pipe HX B) Plate and frame HX C) Shell and tube HX D) Kettle HX
A) Stainless steel B) Copper C) Titanium D) Polymer
A) Trial and error B) Computer simulations C) Expert opinion alone D) Manual calculations only
A) Altering the tube radius B) Changing the fin pitch C) Increasing the number of cores D) Using correction factors
A) Aluminium B) Copper C) Stainless steel D) Carbon steel
A) The uniformity of requirements B) The lack of computer programs C) The simplicity of the process D) The many variables involved
A) Older, less efficient refrigerants B) New generation environmentally friendlier refrigerants C) Water-based solutions D) Non-refrigerant fluids
A) Thermal performance logging B) Hydrostatic pressure testing C) Gas leak testing D) Dye penetration
A) High fluid velocities B) Asphaltene insolubility C) Low wall shear stress D) Cooling water contamination
A) By inhaling through the mouth instead of the nose. B) By exhaling forcefully into the air. C) By wearing a scarf over the face while breathing. D) By removing clothing to expose skin.
A) Nuclear power B) Refrigeration C) Petroleum refining D) Waste water treatment
A) 2040 B) 2028 C) 2025 D) 2030
A) Cross-flow B) Counter-flow C) Parallel-flow D) Mixed-flow |