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a) Hello, in the ```cellulosic model```, the temperature and pressure of ```low-pressure steam``` seems to be higher than the temperature and pressure of ```medium-pressure steam and high-pressure ste…
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I think it is a little difficult to navigate imports and dependencies between biorefinery submodules (e.g., cornstover, sugarcane, lipidcane, and oilcane). Also, although the readme gives basic instru…
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a) Hello, since BioSTEAM does not have ```Chinese investment_site_factors``` (https://biosteam.readthedocs.io/en/latest/API/TEA.html#:~:text=investment_site_factors%3A%20dict%5Bstr%2C%20float%5D%20%3D…
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Hello. I want to import function ```capex_table``` in https://github.com/BioSTEAMDevelopmentGroup/Bioindustrial-Park/blob/master/biorefineries/tea/cellulosic_ethanol_tea.py#L202, I try to import with …
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For the operation cost in the excel file of cellulosic_ethanol model, may I ask you the following questions. I use BioSTEAM 2.43.1.
a) Why is the cost of ```cooling water, chilled water, and low pr…
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a) Hello, if the catalyst needs to be added to the reactor (the actual amount added is large, the catalyst price is also high), but the actual consumption of the catalyst during process operation is v…
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Hi Biosteam community, I'am a new Biosteam user and the first issue I faced up with Biorefineries Bioindustrial-park are the Size of the repo 1.7G, I understand the good practice to share xls files to…
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@yoelcortes, @yalinli2, @sarangbhagwat Hello, could I ask you some questions about the liquid-liquid extraction unit? Thanks for your help.
a) Does the ```partition coefficients``` in the tutorial…
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Hello, may I ask you some questions about HXN? Thanks for your help. Wish you a good day.
a) If there is already heat exchange in the process, such as where ethanol is recovered in cellulosic model…
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Hello, when I execute the following code, it seems that I can not run from the Feedstock unit (```U101```), resulting in ```Water1.F_mass``` is still obtained with the initial mass flow of stream ```E…