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Hello, I built a reactor through class PretreatmentReactorSystem, but after the operation I found net duty of the reactor is zero. In fact, ethanol, sucrose reaction with oxygen should be exothermic r…
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@yalinli2.
I'm running into an issue with negative flow rates in the new high-rate wastewater treatment system. The issue is at the AnMBR. It seems like it requires high moisture contents to work …
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Hello, when I called class PretreatmentReactorSystem, I changed self.reactions.adiabatic_reaction(liquid) in the code to self.reactions(liquid) (https://github.com/BioSTEAMDevelopmentGroup/Bioindustri…
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Hello, I have learned the code for enthalpy calculation and excess enthalpy (https://github.com/BioSTEAMDevelopmentGroup/thermosteam/blob/master/thermosteam/free_energy.py), I have two questions about…
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Hello, I encountered an error while using BioSTEAM: failed to find bracket, it seems that it is caused by ms.vle(T=self.T, V=self.V). I set V=0 because I want to control the gas fraction of outlet str…
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Hi @yoelcortes
I've been trying to use the `oilcane` biorefinery according to the [readme](https://github.com/BioSTEAMDevelopmentGroup/Bioindustrial-Park/tree/master/biorefineries/oilcane#oilcane-…
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Hi @yoelcortes , I noticed some weird with the `RIN_splitter` for the O2 configuration of the oilcane biorefinery, essentially,
```python
>>> from biorefineries import oilcane as oc
>>> oc.load('…
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Hi @yoelcortes , I'm getting really bad MESP numbers now:
```python
>>> from biorefineries import oilcane as oc
>>> oc.load('S1')
>>> oc.sys.TEA.solve_price(oc.ethanol)
554.2055437462008
```
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