wileyonlinelibrary.comresorbable environmental monitors, disposable devices, hardware-secure digital memories, and other applications that are not well served by conventional technologies. [ 1 ] Such types of systems represent a subset of a broader class of a technology referred to as transient electronics. Early work [ 2 ] examined sequentially dissolvable electronics in which variations in the thicknesses and types of the constituent materials determine a time sequence for dissolution across the areas of integrated devices. An important recent advance [ 3 ] in this fi eld followed from the realization of on-demand, triggered dissolution via a remotely controlled microfl uidic system. In the present paper, we demonstrate that these platforms can be extended for use in multistaged transformations of functional behaviors in the transient electronics by means of programmed microfl uidic chemical etching at Electronic systems that enable programmable transformation of functional behaviors by remote control or by autonomous responses to user-defi ned circumstances create unusual engineering opportunities, where physical changes in the hardware induce desired changes in operation. This paper presents materials and device architectures for technologies of this type, in which localized microfl uidic chemical etching of targeted constituent components in the electronics occurs in a sequential, selective manner. Custom circuits that include reconfi gurable radio-powered thermal actuators with analog amplifi ers and square waveform generators illustrate the concepts.
This paper applies
the concept of dynamic intensification (defined
as changes to the dynamics, operation strategy, and/or control of
a process that lead to a substantially more efficient processing path)
to binary distillation columns. The resulting strategy consists of
manufacturing a target product as a blend of two auxiliary products,
both having lower energy demands than a reference value, which corresponds
to producing the target product(s) in a column operating at steady
state. A discussion of the appropriate control structures and switching
strategies between the two auxiliary products is provided. An extensive
case study concerning the separation of a methanol–1-propanol
mixture was carried out, demonstrating that energy savings in the
order of 1.4% are possible with no disruption in product quality or
production rate.
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