System and method for maintaining turbulent flow of mineral spirits for parts flushing
A technology of solvent oil and parts, which is applied in the field of parts washing, can solve the problems of large influence of external factors, inability to realize high-precision parts washing quality, unsatisfactory washing effect, etc., achieve washing temperature balance, strong controllability, and improve washing quality Effect
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Embodiment 1
[0063] This embodiment provides a system for keeping the solvent oil in a turbulent state for parts flushing, such as figure 2 As shown, it includes an operating table 1, a heat exchange subsystem, a temperature control subsystem, a solvent oil circulation subsystem, a water circulation subsystem and a controller, and each subsystem is connected to the controller for coordinated control.
[0064] The operating table 1 provides an operating space for parts flushing, for example, the operating table 1 is provided with a flushing gun head for flushing the parts to be flushed.
[0065] The heat exchange subsystem is used for heat exchange, that is, the heat of the water in the water cycle is uniformly and stably transferred to the solvent oil circulation subsystem, thereby realizing the temperature control of the solvent oil, wherein the heat exchange subsystem at least includes a water / oil heat exchanger 2 , Specifically, the water / oil heat exchanger 2 is a tubular structure.
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Embodiment 2
[0083] This embodiment provides a method for washing parts with solvent oil in a turbulent state, which is implemented by using the system provided in Embodiment 1 above. Specifically, the solvent oil selected for flushing in this embodiment is IsoparL , and its physical properties such as image 3 As shown, according to the liquid viscosity-temperature characteristic equation:
[0084] Vogel equation:
[0085] in:
[0086] is the viscosity at temperature T, is the temperature T 0 The viscosity at , b is a constant, θ is the infinite viscosity temperature, and it can be taken as 95 for standard mineral oil;
[0087] So according to T=25℃: When T=40℃:
[0088] inferred:
[0089] Then the graph of viscosity and temperature is obtained as Figure 4 shown;
[0090] Further, when the flow rate is 1m / s and the pipe diameter is 8mm, the viscosity and Reynolds number of solvent oil at each temperature are shown in the following table:
[0091] temperature...
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