Technical & Practical
Three Insights for Managing Legacy Data
Existing chemical process industries (CPI) facilities possess years, if not decades, of legacy engineering information. The data exist in a myriad of formats and are typically siloed across multiple systems and locations. In cases where the engineering data are either…
Static Electricity Discharge and Fire Prevention
When flammable or combustible atmospheres are present, uncontrolled discharges of static electricity are potentially dangerous or even catastrophic. A significant portion of industrial explosions and fires are attributable to static electricity each year. In theory, controlling static electricity by grounding…
Principles of P&ID Development
The piping and instrumentation diagram (P&ID) is often considered to be the gold standard for the proper design, operation and maintenance of plants in the chemical process industries (CPI), including chemical, oil-and-gas facilities, mining operations, food-processing plants, and water- and…
Production of Bio-based Succinic Acid
Succinic acid is an important industrial chemical that is traditionally derived from petroleum feedstocks. It can be used in several areas — from high-value niche applications, such as food, beverages and pharmaceuticals, to large-volume applications, such as plasticizers, resins and…
Integrally Geared Compressors in the CPI
In an integrally geared centrifugal compressor (Figure 1), several impellers are mounted on the ends of high-speed pinion shafts, which are rotated by a bull-gear. Each impeller’s casing is mounted directly on the horizontally split gear casing. As is the…
Protecting Against Compressor Pulsations
Pressure variations resulting from the oscillatory flow patterns found in positive-displacement machinery, especially reciprocating compressors, are referred to as “pulsations.” Found in both liquid- and gas-handling systems, pulsations are a common phenomenon in the chemical processing industries (CPI). Operational problems…
Mass Transfer in Fermentation Scaleup
How big can a fermenter get? And what would the biggest fermenter look like? The answers to these questions depend upon how the requirements of heat transfer, mass transfer (gas-to-liquid), and momentum transfer (mixing) are met. In an earlier article…
Dilute-phase Pneumatic Conveying: Instrumentation and Conveying Velocity
Dilute-phase pneumatic conveying systems must be operated in a certain sequence and have sufficient instrumentation and operating controls to assure reliable operation and prevent problems. This article discusses two subjects that are important for successful dilute-phase conveying. Discussed below are…
FDA Form 483: Minimizing FDA Inspection Citations
As an owner or manager of a company whose product is regulated by the U.S. Food and Drug Administration (FDA), you will, at some point, be subjected to an FDA inspection. And once an inspection is underway in your facility,…
Methanol-to-Olefins Process
Ethylene and propylene are the most important intermediates in the petrochemical industry. Globally, they are produced mainly by steam cracking of hydrocarbons, such as naphtha, propane and ethane. The methanol-to-olefins (MTO) process is an alternative approach to producing these light…