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Designing a Batch Distillation Unit with Gantt Charts

06/03/2017 By R.C. Costello

Introduction All batch distillation designs start with a Gantt Chart and an annual production rate.  In this example, we'll assume there are three cuts, a lights, a middle cut (or heart cut) and a heavies cut. Batch distillation is time dependent and requires preparation of time cycles on the Gantt chart so that each task can be estimated in minutes and the overall cycle … [Read more...]

Practical Examples of the HOLL-REACTOR® – Part 2

05/11/2017 By R.C. Costello

Part 2 of the Holl-Reactor® In this second installment of the Holl-Reactor®, we will discuss practical applications. Liquid-Liquid Reactions Mixing two liquid reactants is very typical.  This is oftentimes done in a Continuously Stirred Tank Reactor (CSTR).  Depending upon the physical properties of the two liquids, reaction times can be anywhere from minutes to … [Read more...]

The HOLL-REACTOR® for Intensified Chemical Reaction Technology – Part 1

05/01/2017 By Richard Holl

The HOLL-REACTOR® is one of the most important tools in a chemical engineers arsenal for creating smaller processes through process intensification. Molecular Collisions It's obvious that when two liquid reagents are brought into contact with one another, for initiating a chemical reaction, the task of bringing astronomical numbers of reagent molecules into a one-on-one … [Read more...]

Building Reaction Flowsheets Utilizing Process Intensification – Part 2

04/28/2017 By R.C. Costello

In the second part in this 2 part series of Building Reaction Flowsheets Utilizing Process Intensification, we show the production of ethyl silicate utilizing the Shock Wave Power Reactor by Hydrodynamics. This reaction system was originally a packed bed reactor followed by a large CSTR. In addition each reactor had a large distillation column associated with it to separate … [Read more...]

Building Reaction Flowsheets Utilizing Process Intensification – Part 1

04/20/2017 By R.C. Costello

In the first of this two part of the series, we will show two continuous chemical processes that utilize process intensification for chemical reaction systems and unit operations.   The original processes were typically large bulky and spread out over significant plot space and also may have had high profiles. By introducing PI to these technologies a decrease in equipment … [Read more...]

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