<?xml version='1.0' encoding='UTF-8'?><?xml-stylesheet href="http://www.blogger.com/styles/atom.css" type="text/css"?><feed xmlns='http://www.w3.org/2005/Atom' xmlns:openSearch='http://a9.com/-/spec/opensearchrss/1.0/' xmlns:blogger='http://schemas.google.com/blogger/2008' xmlns:georss='http://www.georss.org/georss' xmlns:gd="http://schemas.google.com/g/2005" xmlns:thr='http://purl.org/syndication/thread/1.0'><id>tag:blogger.com,1999:blog-5248613123924336174</id><updated>2026-06-01T06:33:10.640-07:00</updated><category term="excel"/><category term="natural gas"/><category term="solver"/><category term="Goal Seek"/><category term="finite difference"/><category term="heat exchanger"/><category term="pipe"/><category term="reservoir engineering"/><category term="fluid dynamics"/><category term="orifice"/><category term="Bernoulli"/><category term="Haaland"/><category term="ISO 5167"/><category term="LMTD"/><category term="VBA"/><category term="compressibility factor"/><category term="gas"/><category term="heat exchange"/><category term="heat transfer"/><category term="heat transfer area"/><category term="orifice meter"/><category term="two-phase"/><category term="viscosity"/><category term="1D"/><category term="3 reservoir problem"/><category term="API"/><category term="API RP14E"/><category term="ASME Flanged and Dished"/><category term="ASME MFC-14M-2001"/><category term="Bell-Delaware"/><category term="Colebrook-White"/><category term="Dranchuk Abou Kassem"/><category term="Ergun equation"/><category term="Generaux"/><category term="George Stigler"/><category term="Joukowsky Pressure"/><category term="Lockhart"/><category term="Panhandle A"/><category term="Panhandle B"/><category term="Sobocinski-Cornelius"/><category term="Stigler diet"/><category term="Sutherland&#39;s Law"/><category term="TEMA"/><category term="binary distillation"/><category term="brent"/><category term="colburn"/><category term="concentric tube"/><category term="correction factor"/><category term="corrosion"/><category term="cross flow"/><category term="crude oil"/><category term="d exponent"/><category term="darcy-weisbach"/><category term="decline curve analysis"/><category term="diameter"/><category term="dilatant"/><category term="double pipe heat exchanger"/><category term="dynamic viscosity"/><category term="empirical"/><category term="erosion velocity"/><category term="euler"/><category term="exchanger"/><category term="fetkovich"/><category term="flash"/><category term="flow"/><category term="flow regime map"/><category term="fluidized bed"/><category term="friction"/><category term="gas coning"/><category term="gas flow"/><category term="gas viscosity"/><category term="heat equation"/><category term="heat exchaner"/><category term="ideal gas law"/><category term="igt distribution equation"/><category term="igt equation"/><category term="inflow performance relationship"/><category term="iteration"/><category term="least cost"/><category term="linear programming"/><category term="liquid"/><category term="liquid flow"/><category term="log mean temperature difference"/><category term="martinelli"/><category term="mass balance"/><category term="mccabe-thiele"/><category term="meter"/><category term="momentum balance"/><category term="mutlicomponent"/><category term="newtonian"/><category term="ogip"/><category term="oil prices"/><category term="optimized"/><category term="original gas in place"/><category term="packed bed"/><category term="partially filled liquid tanks"/><category term="pde"/><category term="pipeline"/><category term="plot"/><category term="pore pressure"/><category term="pressure drop"/><category term="pressure surge"/><category term="pseudoplastic"/><category term="pump"/><category term="reaction kinetics"/><category term="relative volatility"/><category term="separator"/><category term="shell and tube"/><category term="simplex"/><category term="souders-brown"/><category term="spitzglass equation"/><category term="system curve"/><category term="three reservoir problem"/><category term="vb"/><category term="velocity"/><category term="velocity profile"/><category term="visual basic"/><category term="vle"/><category term="water breakthrough"/><category term="water content"/><category term="water hammer"/><category term="west texas intermediate"/><category term="weymouth equation"/><category term="wti"/><title type='text'>Excel Calculations</title><subtitle type='html'>Free Chemical and Petroleum Engineering Spreadsheets</subtitle><link rel='http://schemas.google.com/g/2005#feed' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/posts/default'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default?redirect=false'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/'/><link rel='hub' href='http://pubsubhubbub.appspot.com/'/><link rel='next' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default?start-index=26&amp;max-results=25&amp;redirect=false'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><generator version='7.00' uri='http://www.blogger.com'>Blogger</generator><openSearch:totalResults>49</openSearch:totalResults><openSearch:startIndex>1</openSearch:startIndex><openSearch:itemsPerPage>25</openSearch:itemsPerPage><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-4176470890506493034</id><published>2013-08-05T16:42:00.001-07:00</published><updated>2013-08-05T17:24:28.822-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="dilatant"/><category scheme="http://www.blogger.com/atom/ns#" term="newtonian"/><category scheme="http://www.blogger.com/atom/ns#" term="pipe"/><category scheme="http://www.blogger.com/atom/ns#" term="pseudoplastic"/><category scheme="http://www.blogger.com/atom/ns#" term="velocity profile"/><title type='text'>Velocity Profile in a Circular Pipe</title><summary type="text">This Excel spreadsheet calculates and plots the velocity profile of a power-law fluid in a circular pipe. The spreadsheet is valid for Newtonian, pseudoplastic and dilatant fluids.




The velocity profile of a Power-law fluid is given by this equation.



where

r is the radial position i.e. distance from the center line (m) 
R is the pipe radius (m)
u(r) is the axial velocity (m s-1)
dp/dz is </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/4176470890506493034/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2013/08/velocity-profile-in-circular-pipe.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/4176470890506493034'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/4176470890506493034'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2013/08/velocity-profile-in-circular-pipe.html' title='Velocity Profile in a Circular Pipe'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEjfoUT6Ni82sA7Nvrq36_MfS_NLgKkZ7Pu6O58O9mKfPeAC4S4q3F2xbi3vhMbqNuDXmrAaP0dgDZ_poq745FKyObflZIIHN4ZxFtrxGl-gjUGKblRf7REUN3Z2wLbHIJlcgPpmU12HL6oM/s72-c/Velocity+profile.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-1454194733714393564</id><published>2013-02-20T18:00:00.002-08:00</published><updated>2013-02-20T18:08:48.169-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="dynamic viscosity"/><category scheme="http://www.blogger.com/atom/ns#" term="empirical"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="gas viscosity"/><category scheme="http://www.blogger.com/atom/ns#" term="ideal gas law"/><category scheme="http://www.blogger.com/atom/ns#" term="Sutherland&#39;s Law"/><title type='text'>Calculate Gas Viscosity with Sutherland&#39;s Law</title><summary type="text">This Excel spreadsheet calculates the viscosity of gasses with Sutherland&#39;s Law. The spreadsheet contains constants suitable for air, but can be used for other gases.




William Sutherland was an Australian scientist who studied the temperature-dependence of ideal gases. In 1893, he developed an empirical-theoretical relationship between the temperature and viscosity of an ideal gas.

</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/1454194733714393564/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2013/02/Gas-Viscosity-Sutherlands-Law.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1454194733714393564'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1454194733714393564'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2013/02/Gas-Viscosity-Sutherlands-Law.html' title='Calculate Gas Viscosity with Sutherland&#39;s Law'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEhlSp-Av1gI9_S5HbVi5J8LOxvggbbTYzjYqBj6g-zzK6_Z-_3OOyHM5x4jBOoJDL_wTAN-L-CPmoQDHkOC96U_LxUt5RX54AU__KyKlBdBF_MAANtHg4Ptc6XUa3EVncJEkLP5qfWqYDNF/s72-c/Sutherland&#39;s+Law+Air+Viscosity.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-1435997007463418058</id><published>2013-02-18T15:27:00.000-08:00</published><updated>2013-02-18T15:27:31.710-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="brent"/><category scheme="http://www.blogger.com/atom/ns#" term="crude oil"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="oil prices"/><category scheme="http://www.blogger.com/atom/ns#" term="VBA"/><category scheme="http://www.blogger.com/atom/ns#" term="west texas intermediate"/><category scheme="http://www.blogger.com/atom/ns#" term="wti"/><title type='text'>Historical Crude Oil Prices</title><summary type="text">These two Excel spreadsheets automatically download historical crude oil prices straight into Excel. Both tools are fully automated; the most you do is supply dates and click a button.

Some VBA then downloads the data from a 3rd party website, straight into Excel. After the data is in Excel, you can do whatever you want - visualize price historical, perform economic analysis, correlate oil </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/1435997007463418058/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2013/02/historical-crude-oil-prices.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1435997007463418058'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1435997007463418058'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2013/02/historical-crude-oil-prices.html' title='Historical Crude Oil Prices'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEgQ__H0Rxy3W_Q2q0hOAeIdYEOUOe07eraEKG06ZLPhMyEl8XVu3r4GhKRtXcgqYZsdzMtQuIr4W7H3Iv9zAIIbBQvqeMAW-go8wDucS5RvmtBVRhSTzT7Omtgghb6iDSfzIpskCA_nxz4/s72-c/WTI+Historical+Prices.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-972190474241486636</id><published>2012-12-16T15:42:00.000-08:00</published><updated>2012-12-16T15:42:04.516-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="heat exchanger"/><category scheme="http://www.blogger.com/atom/ns#" term="heat transfer"/><category scheme="http://www.blogger.com/atom/ns#" term="heat transfer area"/><category scheme="http://www.blogger.com/atom/ns#" term="pipe"/><title type='text'>Heat Loss From An Insulated Pipe</title><summary type="text">This Excel spreadsheet models heat loss from an insulated pipe. This is a very common system in the process industries - insulated pipes are everywhere, and engineers need a sound grasp of heat transfer principles to model their effects.&amp;nbsp;Although the model in the spreadsheet is simplified to aid understanding, complexity can be easily added.



Liquid flows through the pipe, with heat </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/972190474241486636/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/12/heat-loss-from-insulated-pipe.html#comment-form' title='2 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/972190474241486636'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/972190474241486636'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/12/heat-loss-from-insulated-pipe.html' title='Heat Loss From An Insulated Pipe'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEgnlQwqNcvvfmf4cuVasAV-M1VjtpO1GpVi-VElwitAgBq0OLqFLAs4f1mpuVJNT1vUlRFG5b3Yix_V9DKfVC0o7rHZWpyMYKY8E_ZWN8A_mOs27Vm3LtYXbSXSIuCH_XxXp274ZuPhtW6R/s72-c/Insulated+Pipe+Excel.png" height="72" width="72"/><thr:total>2</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-5735083380100128446</id><published>2012-12-08T09:32:00.000-08:00</published><updated>2012-12-08T09:32:06.193-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="d exponent"/><category scheme="http://www.blogger.com/atom/ns#" term="pore pressure"/><category scheme="http://www.blogger.com/atom/ns#" term="reservoir engineering"/><title type='text'>Calculate d-Exponent to Predict Pore Pressure Trends</title><summary type="text">This Excel spreadsheet calculates the d-exponent, a parameter used by drilling engineers to investigate ppore pressure trends when drilling into over-pressurized zones.

Normally, formation density increases with the drilling depth. But if the formation contains sand below the surface, then the drilling rate may increases with drilling depth. The d-exponent is used in several calculations to </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/5735083380100128446/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/12/d-exponent.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/5735083380100128446'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/5735083380100128446'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/12/d-exponent.html' title='Calculate d-Exponent to Predict Pore Pressure Trends'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEib6EfiuIgpBejWu6yggNXFkewV5-Vv6W8Q-AX2wzUUDV64DBwkUKmSyF0_WmpylJJ5CT4mmczd8XkYNzmuEzxvF8m6A5eQA3Iz0KQqOK1CBoSLV8Eoqxg9aVtokjftd9lvEunuuys2OYqB/s72-c/D+exponent+Excel.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-3582430197580721361</id><published>2012-11-21T18:45:00.001-08:00</published><updated>2012-11-21T18:45:05.292-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="finite difference"/><category scheme="http://www.blogger.com/atom/ns#" term="reaction kinetics"/><title type='text'>Modelling Reaction Kinetics in Excel</title><summary type="text">This spreadsheet demonstrates how you can model reaction kinetics in Excel with the solution of differential equations.

Consider this reaction scheme




where A and B are reactants, X and Y are catalysts, and k1 and k2 are rate constants.

The following coupled differential equations can be derived from the stoichiometry of the chemical reaction scheme.




where a(t), b(t), x(t) and y(t) are </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/3582430197580721361/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/11/reaction-kinetics-excel.html#comment-form' title='2 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/3582430197580721361'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/3582430197580721361'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/11/reaction-kinetics-excel.html' title='Modelling Reaction Kinetics in Excel'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEh1DX2tSaj5OByu5fziaJa9krGLHyUPn6BGMFfcNf81w7Ms0Ahh6yWNuQmBHO0r_4-N3zPTLN9nnLiDV8vYT0ERX0YfFKIYitKDc1CoISsEWmrC3cG1TOO38bPFMTxlmbgK1INtN0GG6BV1/s72-c/Reaction+Kinetics+1.png" height="72" width="72"/><thr:total>2</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-6032426979686753691</id><published>2012-10-14T10:36:00.003-07:00</published><updated>2012-10-14T10:52:21.425-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="separator"/><category scheme="http://www.blogger.com/atom/ns#" term="souders-brown"/><title type='text'>Souders-Brown Equation Calculator</title><summary type="text">This Excel spreadsheet calculates the maximum allowable vapor velocity in a vapor-liquid separator with the Souders-Brown equation. The Souders-Brown equation is commonly used to size separators, scrubbers and knock-out drums.

The operating vapor velocity is specified to minimize the entrainment of liquid drops in the exiting vapor.





A wire mesh or de-entrainment pad is commonly used to </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/6032426979686753691/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/10/souders-brown-equation-calculator.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/6032426979686753691'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/6032426979686753691'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/10/souders-brown-equation-calculator.html' title='Souders-Brown Equation Calculator'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEh5e6tAybDyUYcIfH-J7NEJeBFR9YJlEweCLYzBNetLhUvn3YRh5r_rnDi7EZV-miCXS0aNX2N0CUg6FQymwesoB63twZfdniPfCSA39ri8kpOC3rE23I5Lashr6urHBA60RCDO1AoNkjea/s72-c/Souders+Brown+Equation+in+Excel.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-174479437472016185</id><published>2012-09-30T11:10:00.000-07:00</published><updated>2012-09-30T11:10:27.559-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="inflow performance relationship"/><category scheme="http://www.blogger.com/atom/ns#" term="reservoir engineering"/><title type='text'>Inflow Performance Relationship of Vertical &amp; Slanted Solution Gas-Drive Wells</title><summary type="text">This Excel spreadsheet calculates the Inflow Performance Relationship, or IPR, for vertical and slanted solution-gas drive wells.

The IPR of a well determines the relationship between its flowing bottom pressure, and the well production rate (or&amp;nbsp;deliverability).&amp;nbsp;IPR also helps engineers investigate the economics of a well, and is critical in optimizing the well, artificial lift design </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/174479437472016185/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/09/inflow-performance-relationship-of.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/174479437472016185'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/174479437472016185'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/09/inflow-performance-relationship-of.html' title='Inflow Performance Relationship of Vertical &amp; Slanted Solution Gas-Drive Wells'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEgRGGaKKr1ipkzEz1X9cQhfuvNpHPIYqkFvzOJ_1GvREw4iTg-vKC6_H5EHKeq8rl6b62bFYBFHU47F5XzrTvD7xw-90JSPL4ZSRXEoo3NfXjrxt8Ch93jDyoJRud_p0xIhiLEVfAzTEwQ6/s72-c/IPR.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-8086733350386212834</id><published>2012-09-30T08:11:00.002-07:00</published><updated>2013-12-28T18:42:35.401-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="Ergun equation"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="fluidized bed"/><category scheme="http://www.blogger.com/atom/ns#" term="packed bed"/><title type='text'>Ergun Equation Calculator</title><summary type="text">This Excel spreadsheet helps you calculate the pressure drop through packed and fluidizeds bed with the Ergun equation.

Fluidized beds are a commonly unit operation in the process industries. Their nature makes them&amp;nbsp;particularly suitable venues for gas-solid catalyzed reaction, often in the petroleum industry to produce gasoline and other chenicals. They have also found use in the polymer </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/8086733350386212834/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/09/ergun-equation-calculator.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8086733350386212834'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8086733350386212834'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/09/ergun-equation-calculator.html' title='Ergun Equation Calculator'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEgUitnIGedi0X-djGWAryZyrJS2o2A2KYCmeWU796VoB-exRLEhcF4EkuRwdGAxW3mBIpM4A7oC2BoI7MSA0CAYYca53FRqPkSBApbXnoo4GiLzfnFka35Fj_MONoDEuzLt-m-XEBmj-QxM/s72-c/Ergun+Equation.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-7804996403576099223</id><published>2012-09-09T04:43:00.000-07:00</published><updated>2013-06-05T18:32:01.406-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="ASME Flanged and Dished"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="partially filled liquid tanks"/><title type='text'>Liquid Volume in Partially Filled Horizontal Tanks</title><summary type="text">This Excel spreadsheet helps you calculate the liquid volume in partially filled horizontal tanks.

Tanks are often used in storing chemicals. Often, only the liquid height from a level indicator is known. This means you need a method of calculating the liquid volume based on the liquid height and the tank dimensions.




The tank ends can be


flat (so the tank is just a horizontal cylinder)#
</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/7804996403576099223/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/09/volume-partially-filled-tanks.html#comment-form' title='1 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/7804996403576099223'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/7804996403576099223'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/09/volume-partially-filled-tanks.html' title='Liquid Volume in Partially Filled Horizontal Tanks'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEg2Pf6axcsVuaZr0xM_p5iFe9EmZDuWmlopoUUE-wuzB0uxIukaeajAw-dkllbOsuCnkPTclXJxiwqUN_HuwOTnaulqkNEqry0m6PkAv-VDQ7Sn2C2fiuoilNydU5P57u8-XcAK6FctjAv4/s72-c/partially+filled+tank.png" height="72" width="72"/><thr:total>1</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-6788496767735272826</id><published>2012-07-07T06:21:00.005-07:00</published><updated>2012-10-16T02:18:57.589-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="decline curve analysis"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="fetkovich"/><category scheme="http://www.blogger.com/atom/ns#" term="reservoir engineering"/><title type='text'>Fetkovich Decline Curve Analysis</title><summary type="text">This Excel spreadsheet plots Fetkovich decline curves for gas wells.&amp;nbsp;Decline curve analysis is an empirical procedure that predicts the decline in production rates of gas and oil wells.&amp;nbsp;

Fetkovich (1968) improved on earlier work by Arps in predicting the declining production rate of oil and gas wells. He suggested that experimental production rate data could be overlaid on a graph and </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/6788496767735272826/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/07/fetkovich-decline-curve-analysis.html#comment-form' title='1 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/6788496767735272826'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/6788496767735272826'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/07/fetkovich-decline-curve-analysis.html' title='Fetkovich Decline Curve Analysis'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEiznOsayumTgpJ8hkF1HMlKABkiFV0etWQka5V-f72aXdsfmQt9HB_G-b4qhOQFmDs2Y_ax9Jp2udktAIKcVg0t03w3_ORguEcKCI5-7qGygD3Myw-T1K3HBzfSYrLNTFQGvv4TD4Brvugv/s72-c/Fetkovich+Decline+Curve.png" height="72" width="72"/><thr:total>1</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-2658698793329078096</id><published>2012-05-30T11:54:00.000-07:00</published><updated>2012-05-30T11:54:00.417-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="reservoir engineering"/><category scheme="http://www.blogger.com/atom/ns#" term="Sobocinski-Cornelius"/><category scheme="http://www.blogger.com/atom/ns#" term="water breakthrough"/><title type='text'>Water Breakthrough Time in a Vertical Oil Well</title><summary type="text">Consider an oil reservoir with an underlying water zone. An oil well that is producing from this reservoir will experience the phenomenon of water breakthrough if the well produces above its critical rate. Since economic considerations often demand high flowrates, this can be a real risk.




This Excel spreadsheet uses the Sobocinski-Cornelius method to calculate the water breakthrough time. &amp;</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/2658698793329078096/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/05/water-breakthrough-time-in-vertical-oil.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/2658698793329078096'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/2658698793329078096'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/05/water-breakthrough-time-in-vertical-oil.html' title='Water Breakthrough Time in a Vertical Oil Well'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEi1HUoxbPI50tBMLfV_zH9YIIrznFAIZD3YYshhuzDKiD8KmZkLtZ9-04kdqhZC9T_sLBvbJujXqWe9Alq2PkZa1r2DNfGF2C7mrxw8BHkbk2yNalB_58jjfInxeA54sICsbAdPnS8aO5Uk/s72-c/Water+Breathrough+Sobocinski-Cornelius.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-7508517408389855608</id><published>2012-05-13T04:49:00.002-07:00</published><updated>2012-10-16T02:14:11.554-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="binary distillation"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="mccabe-thiele"/><category scheme="http://www.blogger.com/atom/ns#" term="plot"/><category scheme="http://www.blogger.com/atom/ns#" term="relative volatility"/><title type='text'>Binary Distillation with McCabe-Thiele Method</title><summary type="text">This Excel spreadsheet uses the McCabe-Thiele method to calculate the number of theoretical stages needed for binary distillation.

Binary distillation is a common unit operation that separates two liquids (with one being more volatile, or &quot;lighter&quot;). The concepts are encountered in many branches of chemical and petroleum engineering.




Simply enter your parameters at the top of the spreadsheet</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/7508517408389855608/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/05/mccabe-thiele-binary-distillation-excel.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/7508517408389855608'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/7508517408389855608'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/05/mccabe-thiele-binary-distillation-excel.html' title='Binary Distillation with McCabe-Thiele Method'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEidbeM9pG9xPM24Ff2XPkCTpHN5d1gfz1OJOgkAcjl0n_cG4LGV9Y-UyrALvXl9454330E2WOScjaZASrBkDgXYvXsyvIWQ3Uzh7dQuG16dUblo5gGG-vB2RuVhVdMwgzuzWkdl8cYjrTmM/s72-c/Binary+Distillation+McCabe+Thiele.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-7200134540111254335</id><published>2012-02-05T04:41:00.000-08:00</published><updated>2012-02-05T04:43:25.705-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="flow regime map"/><category scheme="http://www.blogger.com/atom/ns#" term="two-phase"/><title type='text'>Flow Regime Map for Two-Phase Flow</title><summary type="text">This Excel spreadsheet plots a flow regime map for the two-phase flow of liquid and gas in horizontal and vertical pipes.



Determining flow regime is important when calculating pressure drops and pumping requirements in the oil &amp;amp; gas industry, and chemical production.&amp;nbsp;Additionally, some flow regimes are undesirable (such as slug flow, which can damage pipes through excessive vibration)</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/7200134540111254335/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/02/flow-regime-map.html#comment-form' title='1 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/7200134540111254335'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/7200134540111254335'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/02/flow-regime-map.html' title='Flow Regime Map for Two-Phase Flow'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEhoNB_ir97ATvReKJgHzFhK1VrkDbmEus_0R4Sfmmr7mTESM9djd-2ESY650dKhIjOYTn7P0SRzN7Fb5m5yjkQqQlEVXsCRLCkRd9xxjtmHJqFsmK6Ny_oW8205ZgMIrGdcDN02oi6NmzcK/s72-c/Flow+Regime+Two+Phase+Flow.png" height="72" width="72"/><thr:total>1</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-178349456825041103</id><published>2012-01-21T05:09:00.000-08:00</published><updated>2012-01-21T06:34:40.230-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="natural gas"/><category scheme="http://www.blogger.com/atom/ns#" term="viscosity"/><title type='text'>Natural Gas Viscosity with Carr, Kobayashi, and Burrows Correlation</title><summary type="text">This Excel spreadsheet uses the Carr, Kobayashi, and Burrows correlation to calculate the viscosity of natural gas. The correlation is valid for sweet and sour gas.

The&amp;nbsp;Carr, Kobayashi, and Burrows correlation was published in 1954. It is valid between temperatures of 32 F to 400 F, reduced pressures below 20, and CO2, N2 and H2S concentrations below 15%.

The correlation was originally </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/178349456825041103/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2012/01/natural-gas-viscosity.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/178349456825041103'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/178349456825041103'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2012/01/natural-gas-viscosity.html' title='Natural Gas Viscosity with Carr, Kobayashi, and Burrows Correlation'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEhfiTS-fHfcdW1DzIPn1E0UACZZRAPPMhawO4jVTwJzYrVSLPE4I25G3SfaUbdwkCwfwAk2iZlGNDA3flTQtC0qAUPL-GSO96p3P49lgvI8xusZQqXy0CRHXSqKYoMu8_wZ3sxGSiDPluIO/s72-c/Carr+Kobayashi+Burrows.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-8329446258034095481</id><published>2011-12-30T04:00:00.000-08:00</published><updated>2011-12-30T04:01:02.652-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="Joukowsky Pressure"/><category scheme="http://www.blogger.com/atom/ns#" term="pressure surge"/><category scheme="http://www.blogger.com/atom/ns#" term="water hammer"/><title type='text'>Water Hammer in Excel</title><summary type="text">This Excel spreadsheet will calculate the maximum pressure surge when the valve at the end of a pipeline is closed. 

When flow is suddenly stopped, flow inertia causes a pressure surge at the valve, with a shockwave propagating through the pipeline. &amp;nbsp;This &amp;nbsp;is also known as Water Hammer and can cause considerable damage. &amp;nbsp;Engineers need to know the maximum pressure surge to </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/8329446258034095481/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/12/water-hammer-excel.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8329446258034095481'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8329446258034095481'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/12/water-hammer-excel.html' title='Water Hammer in Excel'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEga0aIf13hLda8vyprsGN9qi4k3VN8obbZCzuWC_Tp4FyhxcxddjNUR3OO3kR04tpVGutVe-xoRUUMpcwwcv6gAPjbiyJdlmxv1gyJKANQL1WXVMJhQMRFsBVOm1UJJBbMFMtmQPwgBQCwg/s72-c/Water+Hammer.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-3442899926438283457</id><published>2011-12-03T07:42:00.003-08:00</published><updated>2012-10-16T15:24:18.663-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="euler"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="finite difference"/><category scheme="http://www.blogger.com/atom/ns#" term="fluid dynamics"/><category scheme="http://www.blogger.com/atom/ns#" term="friction"/><category scheme="http://www.blogger.com/atom/ns#" term="Haaland"/><category scheme="http://www.blogger.com/atom/ns#" term="liquid flow"/><category scheme="http://www.blogger.com/atom/ns#" term="mass balance"/><category scheme="http://www.blogger.com/atom/ns#" term="momentum balance"/><title type='text'>Dynamic Liquid Flow Between Coupled Tanks</title><summary type="text">This Excel spreadsheet models the transient flow of liquid between two tanks connected by a pipe. &amp;nbsp;Because of the momentum of the liquid, the height of liquid in each tank oscillates to an equilibrium. &amp;nbsp;Flow is opposed by pipe friction, and eventually the liquid level in each tank&amp;nbsp;stabilises.






The dynamics are defined by the following differential equations, which are derived </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/3442899926438283457/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/12/dynamic-liquid-flow-between-coupled.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/3442899926438283457'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/3442899926438283457'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/12/dynamic-liquid-flow-between-coupled.html' title='Dynamic Liquid Flow Between Coupled Tanks'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEgHCPeUlqBX-nVVLnkWrt45gH6f4e_DYmd891_-ZtSO-6LSvcn22GTcO-AHnLATlqTFvy_gmWHta9PFdN5zK-nuZa4w0HtT8LlaXdPsjmm07rnax8MuXcTKM8JQa2HpHAVq_dLjCHpLJf8q/s72-c/CoupledTanks.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-4930300981294315872</id><published>2011-12-02T14:08:00.001-08:00</published><updated>2012-10-16T15:32:21.319-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="darcy-weisbach"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="fluid dynamics"/><category scheme="http://www.blogger.com/atom/ns#" term="solver"/><title type='text'>Darcy-Weisbach Equation for Liquid Velocity in a Pipe</title><summary type="text">This Excel spreadsheet uses the Darcy-Weisbach equation to calculate liquid velocity in a pipe. &amp;nbsp;The Darcy-Weisbach equation describes the relationship between the pressure loss and liquid velocity in a pipe.

This is the equation employed in the spreadsheet.





ΔP is the pressure loss in the pipe (Pa)
ρ is the liquid density (kg m-3)
μ is the liquid viscosity (Pa s)
g is the gravitational</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/4930300981294315872/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/12/darcy-weisbach-liquid-velocity-pipe.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/4930300981294315872'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/4930300981294315872'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/12/darcy-weisbach-liquid-velocity-pipe.html' title='Darcy-Weisbach Equation for Liquid Velocity in a Pipe'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEgqGLxQBIYzX2vxKBjRFQ3M0hgVLsjd3EXLLJHkAE_jhtupYeWvfFwDStVI3Qu2lwZFHumCVw-fBGw2phxQppuASprRHfd3m7rL7tZ4yhTC3U3Y4Z1krIvi_UdcqX9cEhrvcJGgLomEND02/s72-c/Darcy-Weisbach.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-1815647017256300067</id><published>2011-11-30T14:44:00.001-08:00</published><updated>2011-12-01T03:12:58.353-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="Bell-Delaware"/><category scheme="http://www.blogger.com/atom/ns#" term="colburn"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="heat exchanger"/><category scheme="http://www.blogger.com/atom/ns#" term="TEMA"/><title type='text'>TEMA Type E Heat Exchanger Design</title><summary type="text">This Excel spreadsheet helps you design a TEMA Type E heat exchanger. The spreadsheet uses the Bell-Delaware method to calculate the overall heat transfer coefficient and the shell-side pressure drop.

TEMA Type E heat exchangers are the basis of many other designs. They offer a single pass, with liquid entry and exist on opposing sides of the shell

The spreadsheet allows you to pick from a </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/1815647017256300067/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/tema-type-e-heat-exchanger-design.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1815647017256300067'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1815647017256300067'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/tema-type-e-heat-exchanger-design.html' title='TEMA Type E Heat Exchanger Design'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEgijvUghOanmFJvt1zEGG3KFb0PcQ7ASVqOLxgJFDAtdlMz575TOQH6uKUbJrVDFqD3aM9UpYzUdVp1SRUKTh6zvWeMk3IkugEdV2LMEwI5xsgKZerPPwZ9AEVK5e3MPQ3qlAnLc5e_hcd4/s72-c/TEMA+Type+E+Heat+Exchanger.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-4237449421396403042</id><published>2011-11-19T09:21:00.001-08:00</published><updated>2011-11-19T10:58:39.698-08:00</updated><title type='text'>Temperature Dynamics of Heated Tanks Connected in Series</title><summary type="text">This Excel spreadsheet models the temperature dynamics of a feed stream heated in three tanks connected in series. Each tank has a heating coil at a fixed temperature, and it is assumed that each tank is perfectly mixed








The temperature dynamics are modeled by these three differential equations.





M is the mass of liquid in each tank (kg)
T0 is the temperature of the feed stream (K)
T1(</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/4237449421396403042/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/heating-transfer-tanks-series.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/4237449421396403042'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/4237449421396403042'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/heating-transfer-tanks-series.html' title='Temperature Dynamics of Heated Tanks Connected in Series'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEj78BY37uv4EPc42HH6u0vQHh79I4El2J3RRCvE5_59rTmMPmmh8SfOM_JXo3Fqwdm_-CbxlY-MIiXoqvoWFlm2VUHe2KmGFYZq2xYOJNRZSBM6ewkxONJZ6JsfhyHmPULd3oNZHPerKjdB/s72-c/TanksHeat.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-1431115891624478709</id><published>2011-11-16T00:31:00.000-08:00</published><updated>2012-10-16T15:26:28.752-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="concentric tube"/><category scheme="http://www.blogger.com/atom/ns#" term="double pipe heat exchanger"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="Goal Seek"/><category scheme="http://www.blogger.com/atom/ns#" term="heat exchanger"/><category scheme="http://www.blogger.com/atom/ns#" term="heat transfer"/><title type='text'>Double Pipe Heat Exchanger</title><summary type="text">This Excel spreadsheet helps you design a double pipe heat exchanger (also known as a concentric tube heat exchanger). Double pipe heat exchangers are often used in the chemical, food processing and oil &amp;amp; gas industries. They have a particular advantage when close temperature approaches are needed or in high pressure applications.

The spreadsheet will give you important design parameters, </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/1431115891624478709/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/double-pipe-heat-exchanger.html#comment-form' title='6 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1431115891624478709'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/1431115891624478709'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/double-pipe-heat-exchanger.html' title='Double Pipe Heat Exchanger'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEhyzqGVnHoaGnJFKbCmzo9yEdQkySxRtTdWdYJGm0x_kbTgEkdYuEyqodz6CQ-p21uCz-_ZxB-pEc0iN1I6HLOCJCOrNuZI6K-LFjDI0L2tYihquR33pAU-NlPhT1P8SiMOSAFYLsE6IRTd/s72-c/Double+Pipe+Heat+Exchanger+Equations.png" height="72" width="72"/><thr:total>6</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-9048935988259472062</id><published>2011-11-12T14:49:00.000-08:00</published><updated>2011-11-12T15:29:46.479-08:00</updated><title type='text'>Find Orifice Diameter for Specific Operating Parameters</title><summary type="text">These Excel spreadsheets will help you find the orifice size for an orifice flow meter, given various design parameters like the desired pressure drop, fluid properties etc. All the spreadsheets use industry-standard designs, such as ISO&amp;nbsp;5167 and&amp;nbsp;ASME MFC-14M-2001

First, decide what type of orifice you&#39;re designing and download the appropriate Excel Spreadsheet (read the articles for </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/9048935988259472062/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/find-orifice-size.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/9048935988259472062'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/9048935988259472062'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/11/find-orifice-size.html' title='Find Orifice Diameter for Specific Operating Parameters'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEj2mgpegbeJsSJcs6uXMkooKt1uHWDvOLJWJHQ91mPVRsEgTPsw5g1RBed7or8me-EcKXEoE36IqARdmxl2h9IdkupZSuZuuAUCTleddX4QTQxzi5Jn72s1BeEv_jJWXTnMqboSsmQSc4QO/s72-c/Find+Orifice+Size.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-6846805400222368911</id><published>2011-11-07T05:06:00.000-08:00</published><updated>2012-10-16T15:25:39.527-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="gas"/><category scheme="http://www.blogger.com/atom/ns#" term="Goal Seek"/><category scheme="http://www.blogger.com/atom/ns#" term="orifice meter"/><title type='text'>Small-Bore Gas Orifice Meter Flow Calculator</title><summary type="text">This Excel spreadsheet calculates the flowrate from a small-bore gas orifice meter using the&amp;nbsp;ASME MFC-14M-2001 standard. This calculator is valid for pipe diameters of less than&amp;nbsp;40 mm (other restrictions are given below).





The equations are as follows













C is the discharge coefficient. D1&amp;nbsp;has to be supplied in m
D1&amp;nbsp;and D2&amp;nbsp;are the diameter of the pipe and </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/6846805400222368911/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/10/small-bore-gas-orifice-meter-flow.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/6846805400222368911'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/6846805400222368911'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/10/small-bore-gas-orifice-meter-flow.html' title='Small-Bore Gas Orifice Meter Flow Calculator'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEhty7uUgCfIZUxaFL2KEyeSB9GDCvCqXfn9yGXTgREEri7AippwrngHmK_bXjaTJIrPLr_F_3iv2YbpPtPrrEyd_Thu9oGCF_-LHgNPsSOFwzU46wLIrA4tDi5zwFt6VMw5n7sFM8w0Qu0n/s72-c/Small+Bore+Gas+Orifice+Meter.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-8308969738674320538</id><published>2011-11-03T03:54:00.000-07:00</published><updated>2011-11-07T02:52:24.242-08:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="ASME MFC-14M-2001"/><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="orifice"/><category scheme="http://www.blogger.com/atom/ns#" term="orifice meter"/><title type='text'>Small-Bore Liquid Orifice Flow Meter Calculator for Excel</title><summary type="text">This Excel spreadsheet calculates the liquid flowrate from a small-bore orifice meter using the equations defined in&amp;nbsp;ASME MFC-14M-2001. The calculation is iterative, but the spreadsheet is conveniently set up to use Excel&#39;s Goal Seek functionality by simply clicking a button. 




The equations implemented in the spreadsheet are sourced from&amp;nbsp;ASME MFC-14M-2001 and are&amp;nbsp;given below.

</summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/8308969738674320538/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/10/small-bore-orifice-flow-calculator.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8308969738674320538'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8308969738674320538'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/10/small-bore-orifice-flow-calculator.html' title='Small-Bore Liquid Orifice Flow Meter Calculator for Excel'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEjBCUjhtafGDgKE-qTK0tQzE37VgR-1B_jNiEbkYw0vwcnPxnDPmV5iT5JFSNLCaqrRPfZKyfiuiQvNex9Qd2QShllHJ5SgDMNak_Es0-n3fTDyW5jeH-4WXOsC90IW2kgAERWaRRJ9SeyV/s72-c/Small+Diameter+Liquid+Orifice+Meter+Excel.png" height="72" width="72"/><thr:total>0</thr:total></entry><entry><id>tag:blogger.com,1999:blog-5248613123924336174.post-8452110310376483208</id><published>2011-10-29T13:17:00.000-07:00</published><updated>2012-10-16T02:24:39.467-07:00</updated><category scheme="http://www.blogger.com/atom/ns#" term="excel"/><category scheme="http://www.blogger.com/atom/ns#" term="gas coning"/><title type='text'>Critical Oil Flowrate for Gas Coning</title><summary type="text">

This Excel spreadsheet uses the Mayer and Garder correlation to calculate the oil flowrate necessary to form a stable gas cone in an oil and gas reservoir. 

Gas coning references the tendency of gas to flow in the direction in which its face the least resistance, against the flow of gravity.&amp;nbsp; Above the critical oil flowrate, the cone will breakthrough and gas will force the oil flow </summary><link rel='replies' type='application/atom+xml' href='http://excelcalculations.blogspot.com/feeds/8452110310376483208/comments/default' title='Post Comments'/><link rel='replies' type='text/html' href='http://excelcalculations.blogspot.com/2011/10/critical-oil-flowrate-for-gas-coning.html#comment-form' title='0 Comments'/><link rel='edit' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8452110310376483208'/><link rel='self' type='application/atom+xml' href='http://www.blogger.com/feeds/5248613123924336174/posts/default/8452110310376483208'/><link rel='alternate' type='text/html' href='http://excelcalculations.blogspot.com/2011/10/critical-oil-flowrate-for-gas-coning.html' title='Critical Oil Flowrate for Gas Coning'/><author><name>Unknown</name><email>noreply@blogger.com</email><gd:image rel='http://schemas.google.com/g/2005#thumbnail' width='16' height='16' src='https://img1.blogblog.com/img/b16-rounded.gif'/></author><media:thumbnail xmlns:media="http://search.yahoo.com/mrss/" url="https://blogger.googleusercontent.com/img/b/R29vZ2xl/AVvXsEj5ewo6Y3QOrqk6lnPWcQ59e1zKwoE4SfkXvU_E3pBTcoFMfySb3KAG1VPfQ8apXuWkVUfeqKKHSrL0N7OJgUNk7gr5f-BvhtQaCtBCoud3TL-Mx9tGUqcdimtjswmNFA9VknqU1q1EeGQJ/s72-c/Gas+Coning.png" height="72" width="72"/><thr:total>0</thr:total></entry></feed>