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2023-11-18 13:49:50 -0500 | received badge | ● Notable Question (source) |
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2023-05-19 06:34:44 -0500 | marked best answer | DOE commercial building - some issues with Openstudio measure Dear Developers and Engineers, Our research group is going to perform an energy performance enhancement study on existing buildings. We found DOE commercial buildings suitable for our case study since it provides so many comparison opportunities. Our study does not concern with HVAC equipment and control but we need it to be and work based on the latest version of ASHRAE 90.1. We decided to go with OpenStudio measures which simulate the mechanical (HVAC) system as well as constructions. I don't know how these measures work and whether is there any validation process or not. But according to this video, the measure named "Create DOE Prototype Building" was chosen. As we were checking the simulation results, we found out some issues that I need to share with you (LargeOffice-ASHRAE 169-2006-2A):
Regards. PS: I believe I found some problems with the measure. In the IDF file, I found that CLGSETP_SCH_NO_SETBACK Summer Design Day with some setbacks during unoccupied hours is used for sizing calculation. While CLGSETP_SCH_NO_SETBACK Default and CLGSETP_SCH_NO_SETBACK Default|WntrDsn|Sat|Wkdy Day with no set back is used for simulation. I also checked with IDF files provide here and I think I'm right about it. |
2023-05-12 13:48:01 -0500 | received badge | ● Popular Question (source) |
2023-04-12 04:44:04 -0500 | marked best answer | Chiller sequencing In case of having multiple chillers in parallel in chilled water plant loop, some simple control strategy could be considered: Uniform: In this control strategy, each chiller would make same load part. Sequencing: In this control strategy, the first chiller would work at its highest PLR and then the other chiller and the other and... Currently, I am working with OpenStudio. I chilled water loop tab, there is a part for controlling. An availability manager part can be seen but, I don't know how to use it and I don't know if it's capable of preforming mentioned control strategies. 1- Can anyone help me with this? 2- I have another question related to this. Is it possible in each timestep we determine how many chillers to use and what control strategy to use? |
2023-02-11 06:33:26 -0500 | marked best answer | Phase Change Material (PCM) storage in EnergyPlus Hi, I know EnergyPlus already contains ice storage and cold water storage tank. In my research, I need to study and test phase change material like paraffin waxes or bioPCMs. Is there any way to change ice storage tank properties in order to change its behavior to the PCM storage tank? if not, I would appreciate any help! |
2022-09-01 23:28:37 -0500 | received badge | ● Taxonomist |
2021-03-15 13:10:12 -0500 | marked best answer | Coupling MATLAB(or SIMULINK) with EnergyPlus? If it's possible for you, please share any document (theses, paper, etc) that provides (detailed) information about coupling EnergyPlus and MATLAB. I already know about bctvb main tutorial. I need some more practical, case study and exemplary ones. |
2021-02-02 11:16:18 -0500 | marked best answer | Is it accurate for the large office prototype models to use zone multipliers? I have a problem with the geometry of the DOE reference building. I loaded the model by OpenStudio measure and in the Geometry tab of OpenStudio, it shows only three floors! I realized that the model multiplies middle zones by 10 to simulate floors between top and basement floor. As long as there is no lighting study, Is it valid to do such a thing? Is it enough that the middle floor's ceiling has an appropriate boundary condition? |
2020-12-09 11:49:12 -0500 | marked best answer | Integrated Part Load Value (IPLV) calculated is not at the AHRI test condition! I'm using the default openstudio curve setting for chillers in DOE reference buildings simulation to cool an ice storage tank. I have to set chiller output temperature to negative values (e.g. -5). The simulation completed successfully but here is a warning that concerns me: I'm not familiar with IPLV variable and how important it is... This chiller is not specially selected for ice-making applications and that might be a problem. Since I'm studying a non-standard cooling system, Is this warning important or not? |
2020-12-09 09:12:20 -0500 | commented question | Pumping system / Plant Convergence issue @Julien Marrec, Thank you. I tried ramping down the setpoint but that couldn't help. Here is a detailed output variable |
2020-12-09 07:37:58 -0500 | edited question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus works with just a fe |
2020-12-09 07:35:58 -0500 | edited question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus works with just a fe |
2020-12-08 22:43:03 -0500 | edited question | Trouble getting variable handle in PythonPlugin Trouble getting variable handle in PythonPlugin I'm having trouble getting some variable handles using PythonPlugin in e |
2020-12-08 20:52:38 -0500 | edited question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus works without any wa |
2020-12-08 20:40:35 -0500 | edited question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus works without any wa |
2020-12-08 20:30:59 -0500 | edited question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus works without any wa |
2020-12-08 18:38:39 -0500 | edited question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus works without any wa |
2020-12-08 18:38:27 -0500 | edited question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus works without any wa |
2020-12-08 18:36:47 -0500 | asked a question | Pumping system / Plant Convergence issue Pumping system / Plant Convergence issue The following configuration of cooling loops in energyplus worrks without any w |
2020-12-08 18:06:57 -0500 | edited question | Why does my simulation terminates in the middle of simulation (7h month)) Why does my simulation terminates in the middle of simulation (7h month)) Hi everyone, I am having the following error. |
2020-12-08 00:35:02 -0500 | marked best answer | How can I set Heat exchanger fluil-to-fluid supply side outlet temperature? I using primary and secondary loops to provide cooling in my case. A The green temperatures are my desired temperatures and the red ones with plenty of error are ones that I get! |
2020-12-07 23:40:10 -0500 | edited question | Can anyone tell me why my Openstudio model in SketchUp keeps going white? Can anyone tell me why my open studio model in SketchUp keeps going white? I never save through SketchUp and only open i |
2020-12-07 23:37:49 -0500 | answered a question | Can anyone tell me why my Openstudio model in SketchUp keeps going white? I think when you start to work with the openstudio application, you are actually adding some objects that the openstudio |
2020-12-07 16:03:36 -0500 | answered a question | How to change CHP type? Hi @kimiya, in my opinion, each CHP system should be optimized separately. There would be no point in optimization if yo |
2020-12-07 03:26:22 -0500 | commented answer | Trouble getting variable handle in PythonPlugin Just to be clear, output:variable reporting frequency doesn't matter for the plugin. |
2020-12-06 10:30:42 -0500 | marked best answer | Trouble getting variable handle in PythonPlugin I'm having trouble getting some variable handles using For example here is what I got in the *.rdd file: and here is what I used in my python script to get the handle: Unfortunately, the API returns -1 value for this variable and some other variables. I can't figure out what's the problem. It seems that all the variables listed in the *.rdd file cannot be handled by PythonPlugin. If I'm right, how can one identify available variables(sensors) for each model? I hope that you can help me with this. P.S. |
2020-12-06 00:59:33 -0500 | commented question | [bcvtb],inputs and outputs energyplus and systemcommand You need to read the EMS manual. No one here would not do that for you :) Also, I recommend you to ask you bcvtb related |
2020-12-06 00:53:29 -0500 | edited question | How can I get unmet hours during the simulation? How can I get unmet hours during the simulation? In order to reduce the computational load during the optimization of my |
2020-12-06 00:53:17 -0500 | asked a question | How can I get unmet hours during the simulation? How can I get unmet hours during the simulation? In order to reduce the computational load during the optimization of my |
2020-12-06 00:29:29 -0500 | edited question | [bcvtb],inputs and outputs energyplus and systemcommand [bcvtb],inputs and outputs energyplus and systemcommand Hello I am trying to connect idf to system command (Compiled cpp |
2020-12-05 23:11:47 -0500 | edited answer | How can I create a virtual load to activate supply side of plant? Here is a solution my friend. After autosizing components in the plant loop that you intend to use your virtual load, re |
2020-12-05 23:10:09 -0500 | answered a question | How can I create a virtual load to activate supply side of plant? Here is a solution my friend. After autosizing components in the plant loop that you intend to use your virtual load, re |
2020-12-05 03:12:27 -0500 | commented question | How can I create a virtual load to activate supply side of plant? @Julien Marrec, Where should I use it? I didn't get your point. Actually, I got the idea of the virtual load from a pape |
2020-12-04 13:54:59 -0500 | marked best answer | Inconsistency in curve calculations I found a problem with the curve input/output in my model. The curve is used for chiller performance (EirFTemp). I have reported the following variables: (since I'm using Columns with same color should have a same value (at least with a time lag!). But they are much different specially for the chiller outlet temperature. Why the input 1 of the curve is different from chiller outlet temperature?! Where does it come from?! Update: I should mention that it happens mostly when the chiller outlet temperature setpoint is negative (e.g. -5). Update (following my response to Julien): I think I narrowed down the problem. The |
2020-12-04 13:54:46 -0500 | commented answer | Inconsistency in curve calculations Thank you @julien Marrec for your time. I really appreciate it. You are absolutely right about capacity function of temp |
2020-12-03 18:44:08 -0500 | commented question | Ice Storage Controls Hi @bbrannon4, I hope you're doing well. I wonder if you have any ice-making chiller curve data available. I would reall |
2020-12-03 18:44:01 -0500 | commented question | Ice Storage Controls Hi @bbrannon4, I hope you're doing well. I wonder if you have any ice-making chiller curve data available. I would reall |
2020-12-03 18:38:38 -0500 | commented question | ice storage in openstudio does not change results Dear @hj630 , I am working on a similar project with academic goals. Can you share your experience with Ice storage mode |
2020-12-03 17:21:41 -0500 | commented question | Ice Storage Controls Hi @bbrannon4, I hope you're doing well. I wonder if you have any ice-making chiller curve data available. I would reall |
2020-12-03 17:21:23 -0500 | commented question | Ice Storage Controls Hi bbrannon4, I hope you're doing well. I wonder if you have any ice-making chiller curve data available. I would really |
2020-12-03 16:42:56 -0500 | received badge | ● Associate Editor (source) |