Technical & Practical
Prevent Combustible Dust Explosions with Nitrogen Inerting
Targeted use of blanketing with inert gas offers an effective strategy for preventing combustible dust explosions in CPI facilities Combustible dust is a critical safety concern for the chemical process industries (CPI). The use of nitrogen gas as an inert…
“Green” Ethylene Production Provided by Intratec Solutions
With a global nominal capacity of about 140 million ton/yr, ethylene is among the main petrochemicals produced worldwide, and is a key building block for the industry. Ethylene is produced mostly via steam-cracking of petroleum-based feedstocks, such as naphtha. Ethylene…
Dimensionless numbers in fluid dynamics
Dimensionless numbers refer to physical parameters that have no units of measurement. These numbers often appear in calculations used by process engineers. As long as consistent units are used, dimensionless numbers remain the same whether metric or other units are…
Flare Consolidation Considerations
Consolidating multiple flares can help mitigate emissions and maintenance Chris Ng and Zubin Kumana Siemens, Process Safety Consulting Many petroleum-refining and petrochemical facilities have experienced tremendous growth in recent years in response to increasing demand for fuels and chemical precursors.…
Bulk Solids: Optimizing Screw Conveyors
Despite their apparent simplicity, the complexity of these conveying systems demands proper design and an understanding of the underlying principles Screw conveyors play a major role in a wide variety of industrial operations that involve the handling of bulk solids.…
Thermal Design Guidelines for Optimizing Shell-and-Tube Heat Exchangers
Ensuring optimal performance of shell-and-tube heat exchangers requires knowledge of the controlling fluid, correct exchanger geometry and configuration, as well as proper fluid placement Satyendra Kumar Singh Simon India Ltd. Optimizing the thermal design of a shell-and-tube heat exchanger…
Evaluate Heat-Exchanger Tube-Rupture Scenarios Using Dynamic Simulation
Applying dynamic simulation models to tube-rupture scenarios can help ensure more accurate sizing and hazard assessments Tube rupture in heat exchangers is an extremely serious issue in the chemical process industries (CPI; Figure 1). Heat-exchanger tube-rupture scenarios can be evaluated…
Technology Profile: Sugar Inversion
The substance known colloquially as table sugar is actually sucrose, a disaccharide composed of fructose and glucose. Sucrose is a major agriculturally derived product with an established industry for its extraction, processing and supply. It is mainly employed as a…
The Impact of Off-BEP Pump Operation
Best-efficiency point (BEP), the flowrate at which a pump operates at its highest or optimum efficiency for a specific impeller diameter, is a key consideration when assessing pump performance. While most pumps do not consistently operate at their exact BEP,…
Plot Plan Design: Process Requirements
It is important to conceptualize plant layout in terms of both ideal location and optimal geographical positioning of equipment components For any chemical process facility, the cost of improper or sub-obtimal plant layout can be enormous. Designers are generally well…