Yearly Archives: 2009

Variation of properties in the dense phase region; Part 1 – Pure Compounds

Written on December 1, 2009 at 3:50 pm, by

In this tip of the month (TOTM) we will describe the dense phase of a pure compound, what it is, and how it impacts processes. We will illustrate how thermophysical properties change in the dense phase as well as in the neighboring phases. The application of dense phase in the oil and gas industry willContinue Reading

Three Simple Things to Improve Process Safety Management

Written on November 1, 2009 at 3:47 pm, by

In this Tip of the Month, we look at how to deal with some of the challenges of managing process safety.  This TOTM is an excerpt of a paper presented by JMC Instructor/Consultant, Clyde Young at the 2008 Mary K. O’Connor Process Safety Symposium.  This TOTM continues where the February 2009, TOTM left off. Processes areContinue Reading

Considering the effect of crude oil viscosity on pumping requirements

Written on October 1, 2009 at 3:30 pm, by

In the August 2009 Tip of the Month (TOTM), it was shown that pumping power requirement varies as the crude oil °API changes. Increasing °API or line average temperature reduces the crude oil viscosity. The viscosity reduction caused higher Reynolds number, lower friction factor and in effect lowered pumping power requirements. Since the objective ofContinue Reading

How to Tune the EOS in your Process Simulation Software?

Written on September 1, 2009 at 10:36 pm, by

Process simulation computer programs are excellent tools for designing or evaluating gas processing plants, chemical plants, oil refineries or pipelines. In these simulation programs, most of the thermodynamic properties are calculated by an equation of state (EOS). The cubic equations of state can be regarded as the heart of these programs for generating the requiredContinue Reading

How sensitive are crude oil pumping requirements to viscosity?

Written on August 1, 2009 at 10:31 pm, by

During the life cycle of a crude oil pipeline the properties of transported oil change, because in gathering systems the produced oils come from different wells. New wells may be added or some wells may go out of production for maintenance and repair. Production rates during the life of wells vary, too. In addition theContinue Reading

Variation of Natural Gas Heat Capacity with Temperature, Pressure, and Relative Density

Written on July 1, 2009 at 10:23 pm, by

The change in enthalpy for a fluid where no phase change occurs between Points (1) and (2) can be expressed as: (1) The second term on the right hand side of this equation is generally not convenient to solve manually. However, it is trivial or zero for the following cases: (1) ideal gases, (2) constantContinue Reading

Corrosion Monitoring and Inspection – Is There a Difference?

Written on June 1, 2009 at 10:20 pm, by

Introduction To many people involved in the Oil and Gas production and refining industry, the terms monitoring and inspection are used interchangeably when referring to corrosion issues. However, this lack of differentiation can lead to misunderstandings and errors.  It is our contention that a clear differentiation is needed and that engineers should strive to useContinue Reading

The Sensitivity of k-Values on Compressor Performance

Written on May 1, 2009 at 10:07 pm, by

One of the most important physical properties of a gas is the ratio of specific heats.  It is used in the design and evaluation of many processes.  For compressors, it is used in the design of components and determination of the overall performance of the machine.  Engineers are frequently asked to evaluate a compressor performanceContinue Reading

Quick Determination of the Methanol Injection Rate for Natural-Gas Hydrate Inhibition

Written on April 1, 2009 at 9:51 pm, by

The formation of hydrates in processing facilities and pipelines has been a problem to the natural gas industry. Whether the problem occurs in transportation or processing, hydrate formation can cause shutdowns and even destruction of valuable equipment. Because of these devastating and often costly consequences of hydrate formation, methods have been applied to prevent hydrateContinue Reading

How sensitive is pressure drop due to friction with roughness factor?

Written on March 1, 2009 at 9:23 pm, by

In the February 2007 tip of the month (TOTM), Joe Honeywell [1] presented a procedure for calculating fluid pressure drop for liquid in a piping system due to friction. Continuing Honeywell’s TOTM, we will outline procedures for calculation of friction losses in oil and gas pipelines. From an engineer’s point of view the question may arise “howContinue Reading