{"id":469,"date":"2011-03-09T21:19:52","date_gmt":"2011-03-09T21:19:52","guid":{"rendered":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/?page_id=469"},"modified":"2012-12-07T11:22:56","modified_gmt":"2012-12-07T17:22:56","slug":"full-tip-of-the-month-archives","status":"publish","type":"page","link":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/full-tip-of-the-month-archives\/","title":{"rendered":"Full Tip of the Month Archives"},"content":{"rendered":"

November 2012
\nSolubility of Acid Gases in TEG Solution: Part 3 (CO2 in TEG)\u00a0<\/a><\/p>\n

October 2012
\nShould unplanned maintenance jobs be recorded as near misses?<\/a><\/p>\n

September 2012
\nLow Pressure Versus High Pressure Dense Phase Natural Gas Pipeline Transportation\u00a0<\/a><\/p>\n

August 2012
\nTransportation of Natural Gas in Dense Phase\u00a0<\/a><\/p>\n

July 2012
\nSolubility of Acid Gases in TEG Solution: Part 2\u00a0<\/a><\/p>\n

June 2012
\nSolubility of Acid Gases in TEG Solution<\/a><\/p>\n

May 2012
\nImpact of Non-Hydrocarbons on the Reservoir Fluids Phase Envelope\u00a0<\/a><\/p>\n

April 2012
\nNatural Gas with Dry Ice Phase Behavior<\/a><\/p>\n

March 2012
\nEffect of Nitrogen Impurities on CO2 Dense Phase Transportation<\/a><\/p>\n

February 2012
\nNon-Isothermal Transportation of CO2<\/sub> in the Dense Phase<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

January 2012
\nTransportation of CO2<\/sub> in Dense Phase<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

December 2011
\nWhich Equations of State Should be Used for Compressor Calculations?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

November 2011
\nCompressor Calculations: Rigorous Using Equation of State vs Shortcut Method<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

October 2011
\nLiquid Density by Volume Translated Method \u2013 Part 3: Light Hydrocarbon Mixtures<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

September 2011
\nAnalyzing Engineering Tasks to Minimize or Eliminate Mistakes<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

August 2011
\nA Simple Model for Estimation of Methanol Loss to Vapor Phase<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

July 2011
\nLiquid Density by Volume Translated Method \u2013 Part 2: Recent Development<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

June 2011
\nAbsorption of Aromatics Compounds in TEG Dehydration Process<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

May 2011
\nEstimation of Methanol Loss to Vapor Phase<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

April 2011
\nA Simplified, Graphical Representation of Process Safety Competency Development<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

March 2011
\nLiquid Density by Volume Translated Method \u2013 Part 1: Pure Compound<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

February 2011
\nWhy NPSHR Changes With Impeller Diameter?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

January 2011
\nWhat is the Impact of Water Content on the Dew Point and Hydrate Phase Behavior?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

December 2010
\nShould the TEG Dehydration Unit Design Be Based on the Water Dew Point or Hydrate Formation Temperature?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

November 2010
\nProcess Analysis of Hydrogen Blistering in NGL Fractionation Unit<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

October 2010
\nDetermination of Traces of Methanol in the TEG Dehydrated Gas<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

September 2010
\nImportant Aspects of Centrifugal Compressor Testing – Part 2<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

August 2010
\nImportant Aspects of Centrifugal Compressor Testing-Part 1<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

July 2010
\nThe Hybrid Hydrate Inhibition-Part 2: Synergy Effect of Methanol and KHI<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

June 2010
\nThe Hybrid Hydrate Inhibition<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

May 2010
\nDistribution of Sulfur-Containing Compounds in NGL Products by Three Simulators<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

April 2010
\nThree Simple Things to Improve Process Safety Management<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

March 2010
\nThe parameters affecting a phase envelope in the dense phase region<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

February 2010
\nDistribution of Sulfur-Containing Compounds in NGL Products<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

January 2010
\nVariation of properties in the dense phase region; Part 2 \u2013 Natural Gas<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

December 2009
\nVariation of properties in the dense phase region; Part 1 – Pure Compounds<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

November 2009
\nThree Simple Things to Improve Process Safety Management<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

October 2009
\nConsidering the effect of crude oil viscosity on pumping requirements<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

September 2009
\nHow to Tune the EOS in your Process Simulation Software?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

August 2009
\nHow sensitive are crude oil pumping requirements to viscosity?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

July 2009
\nVariation of Natural Gas Heat Capacity with Temperature, Pressure, and Relative Denisty<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

June 2009
\nCorrosion Monitoring and Inspection \u2013 Is There a Difference?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

May 2009
\nThe Sensitivity of k-Values on Compressor Performance<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

April 2009
\nQuick Determination of the Methanol Injection Rate for Natural-Gas Hydrate Inhibition<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

March 2009
\nHow Sensitive is Pressure Drop Due to Friction With Roughness Factor?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

February 2009
\nThree Simple Things to Improve Process Safety Management<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

January 2009
\nPressure Relief System Design Pit-falls<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

December 2008
\nMaintenance Fallacy:\u00a0 Focusing on Maintenance Planning and Scheduling and Reliability Will Increase Reliability Quickly<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

November 2008
\nEffect of gas molecular weight on centrifugal compressor performance<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

October 2008
\nHow good are the detailed methods for sour gas density calculations?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

September 2008
\nHow good are the shortcut methods for sour gas density calculations?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

August 2008
\nHow good is Flanigan Correlation for Two Phase Gas-Liquid Pipeline Calculations?<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

July 2008
\nThe Truth about Why Your Preventive Maintenance Program Isn\u2019t Working<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

June 2008
\nTwo Phase Gas-Liquid Pipeline Simulation<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

May 2008
\nFlash Tank vs. HEX Economizer Refrigeration System<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

April 2008
\nProviding a safe work place is good business: Learn from experience<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

March 2008
\nEffect of Impurities on Propane Refrigeration System \u2013 Constant Approach Temperature<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

February 2008
\nEffect of Impurities on Propane Refrigeration System<\/a> | (Espa\u00f1ol<\/a>)<\/p>\n

January 2008
\nRefrigeration with Flash Economizer vs Simple Refrigeration System<\/a><\/p>\n

December 2007
\nAcid Gas-Water Phase Behavior<\/a><\/p>\n

November 2007
\nWater-Sour Natural Gas Phase Behavior<\/a><\/p>\n

October 2007
\nWater-Sweet Natural Gas Phase Behavior<\/a><\/p>\n

September 2007
\nConsequence of Liquid Carry Over \u2013 Part 2: Fixed Heat Exchanger Area<\/a><\/p>\n

August 2007
\nVigilance in Outside Contracting<\/a><\/p>\n

July 2007
\nConsequence of Liquid Carry Over in a Simple Dew Point Control Plant<\/a><\/p>\n

June 2007
\nWhy do I care about phase diagrams?<\/a><\/p>\n

May 2007
\nVigilance With a Healthy Dose of Fear<\/a><\/p>\n

April 2007
\nMEG Dehydration Ability in MEG Injection Plant<\/a><\/p>\n

March 2007
\nMEG Injection vs. TEG Dehydration<\/a><\/p>\n

February 2007
\nFriction Pressure Drop Calculation<\/a><\/p>\n

January 2007
\nGuidelines for Liquid Density Prediction \u2013 Part 2: Process Simulator<\/a><\/p>\n

December 2006
\nGuidelines for Liquid Density Prediction \u2013 Part 1: Correlations<\/a><\/p>\n

November 2006
\nLiquid Density<\/a><\/p>\n

October 2006
\nGuidelines for Selecting K-Value Method<\/a><\/p>\n

September 2006
\nHow to determine K-Values?<\/a><\/p>\n

August 2006
\nEffect of Viscosity on Pump Performance<\/a><\/p>\n

July 2006
\nAccuracy of Three Shortcut Prediction Methods for Hydrate Inhibition<\/a><\/p>\n

June 2006
\nAccuracy of Commercial Process Simulators for Hydrate Inhibition<\/a><\/p>\n

May 2006
\nBetter Alternative for Natural Gas Sweetening<\/a><\/p>\n

April 2006
\nThe Impact of Insulation on Pipeline Performance<\/a><\/p>\n

March 2006
\nHydrate Inhibition<\/a><\/p>\n

February 2006
\nHow to Regenerate Adsorption Tower Effectively?<\/a><\/p>\n

January 2006
\nFinding the Optimum Compressor Interstage Pressure<\/a><\/p>\n

December 2005
\nImpact of Liquid Carry Over on Sales Gas Dew Point<\/a><\/p>\n

November 2005
\nSelecting the Correct Phase Envelope<\/a><\/p>\n

October 2005
\nHow to Characterize the Heavy Ends?<\/a><\/p>\n

September 2005
\nHow to Generate a Phase Envelope?<\/a><\/p>\n

August 2005
\nWhere did my Compressor Power Go?<\/a><\/p>\n

July 2005
\nAreas of Risk in the Operation or Design<\/a><\/p>\n

June 2005
\nWhy do I care about phase diagrams?<\/a><\/p>\n","protected":false},"excerpt":{"rendered":"

November 2012 Solubility of Acid Gases in TEG Solution: Part 3 (CO2 in TEG)\u00a0 October 2012 Should unplanned maintenance jobs be recorded as near misses? September 2012 Low Pressure Versus High Pressure Dense Phase Natural Gas Pipeline Transportation\u00a0 August 2012 Transportation of Natural Gas in Dense Phase\u00a0 July 2012 Solubility of Acid Gases in TEG […]<\/p>\n","protected":false},"author":1,"featured_media":0,"parent":0,"menu_order":0,"comment_status":"open","ping_status":"open","template":"","meta":{"nf_dc_page":"","_monsterinsights_skip_tracking":false,"_monsterinsights_sitenote_active":false,"_monsterinsights_sitenote_note":"","_monsterinsights_sitenote_category":0,"footnotes":""},"coauthors":[17],"class_list":["post-469","page","type-page","status-publish","hentry"],"jetpack_shortlink":"https:\/\/wp.me\/P1pQc4-7z","jetpack_sharing_enabled":false,"_links":{"self":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/pages\/469","targetHints":{"allow":["GET"]}}],"collection":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/pages"}],"about":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/types\/page"}],"author":[{"embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/users\/1"}],"replies":[{"embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/comments?post=469"}],"version-history":[{"count":26,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/pages\/469\/revisions"}],"predecessor-version":[{"id":3072,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/pages\/469\/revisions\/3072"}],"wp:attachment":[{"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/media?parent=469"}],"wp:term":[{"taxonomy":"author","embeddable":true,"href":"http:\/\/www.jmcampbell.com\/tip-of-the-month\/wp-json\/wp\/v2\/coauthors?post=469"}],"curies":[{"name":"wp","href":"https:\/\/api.w.org\/{rel}","templated":true}]}}