TNT Melt-Casting

The properties of an oxy-acetylene flame are controlled by the volumetric ratio of oxygen to acetylene. A neutral flame (ratio ≈ 1.1:1) is standard for steel welding. A carburizing or reducing flame (ratio 1.1:1) has excess oxygen, is hotter, and is used for braze-welding.

Gas cylinders for oxy-fuel welding store gases or other industrial or medical gases, at very high pressures. A pressure regulator is essential to reduce this to a safe, usable working pressure. A two-stage regulator performs this reduction in two steps, providing a highly constant delivery pressure even as the cylinder pressure drops with use. This ensures a stable flow, thus a stable flame for consistent weld quality.

Acoustic impedance (\(Z\)) is a material's intrinsic resistance to acoustic flow, defined as its density (\(\rho\)) multiplied by its acoustic velocity (\(c\)), so \(Z = \rho c\). The percentage of ultrasonic energy reflected at the boundary between two materials is governed by the difference, or mismatch, in their respective acoustic impedances. This principle is what makes flaw detection possible.

Engine knock, or detonation, is a major constraint on the thermal efficiency of an Otto cycle engine. While higher compression ratios increase efficiency, they also raise the temperature and pressure of the air-fuel mixture during compression. This can cause the mixture to auto-ignite prematurely, creating a shockwave that produces a 'knocking' sound and can damage the engine.

This equation describes the motion of vehicles that follow the basic principle of a rocket: a device that can apply acceleration to itself by expelling part of its mass with high velocity. It relates the delta-v a rocket can achieve to its effective exhaust velocity and the initial and final mass, given by \(\Delta v = v_e \ln \frac{m_0}{m_f}\).

Oxy-fuel cutting, or flame cutting, severs ferrous metals by a rapid, exothermic oxidation process. First, a preheating flame raises the steel's surface to its kindling temperature (approx. 870 °C or 1600 °F). A high-pressure jet of pure oxygen is then directed at the spot, initiating a chemical reaction, \(3Fe + 2O_2 \rightarrow Fe_3O_4\), which forms molten iron oxide (slag) and releases heat.

The separation factor, α (alpha), quantifies the selectivity of an extraction system for two different solutes, A and B. It is defined as the ratio of their individual distribution ratios, \(\alpha_{A,B} = \frac{D_A}{D_B}\). For a separation to be effective, α must be significantly different from unity. A larger α value implies an easier and more efficient separation.

The Log Mean Temperature Difference (LMTD) is the effective mean temperature difference for heat transfer in heat exchangers, particularly for counter-flow and parallel-flow arrangements. It is a logarithmic average of the temperature difference between the hot and cold fluids at each end. The LMTD is calculated using the formula: \(\Delta T_{LM} = \frac{\Delta T_A - \Delta T_B}{\ln(\Delta T_A / \Delta T_B)}\).

Temper embrittlement is a reduction in the toughness of certain alloy steels caused by holding them in, or slowly cooling them through, a specific temperature range (approximately 375–575 °C). This phenomenon is driven by the segregation of impurity elements (e.g., phosphorus, tin, antimony) to the grain boundaries, which weakens the cohesion between grains and promotes intergranular fracture.

For materials that do not have a distinct yield point on their stress-strain curve, like aluminum or high-strength steel, 'proof stress' is the engineering equivalent. It is defined as the stress required to produce a small, specified amount of permanent (plastic) deformation, typically 0.2% of the original gauge length. This value, \(\sigma_{0.2}\), is used in design calculations as the material's practical elastic limit.

Fouling is the accumulation of unwanted material on heat transfer surfaces, which introduces an additional thermal resistance and degrades the performance of a heat exchanger. This fouling resistance (\(R_f\)) reduces the overall heat transfer coefficient (U). The effect is quantified in the overall heat transfer equation: \(\frac{1}{U} = \frac{1}{h_i} + \frac{1}{h_o} + R_f + R_w\).