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The IDAES Process Systems Engineering Framework

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## Fixes NA ## Summary/Motivation: These changes provide utility functions which allow the user to create pruning and sparsification routines for keras surrogates. ## Changes proposed in this PR: -...

Priority:Normal

Right now, some IDAES models obtain an initial condition for a model with dynamics by adding logic constraining the first time point to be at steady state. See, for example,...

Priority:Normal

Noticed the following bug while working on the unit model tutorial with @anujad95. - If Q is fixed as part of the initial specifications, and `initialize()` is called --> initialization...

bug
Priority:Normal
IDAES v2.0

In 1-D control volumes, and some property package state blocks, equations are often skipped at the inlet (or points where `defined_state is True` in state blocks). This causes some inconveniences/problems...

enhancement
Priority:Low
core

## Summary/Motivation: Wanted to try out the shot-scraper package ## Changes proposed in this PR: - scripts and stuff in docs/screenshot/ - ### Legal Acknowledgement By contributing to this software...

Priority:Normal

We need to macOS binaries for completeness in our install instruction coverage. We have ARM64 binaries now is that sufficient? If we need x86_64, how are we going to get...

Priority:High

*Note on organization*: I'll update this top post as my understanding of the issue evolves. Posts in the comment thread document my debugging steps. **Overall problem:** `idaes get-extensions` is not...

Priority:Normal

If you try doing the same `m.fs.visualize()` call in e.g. the HDA flowsheet with distillation, both before and after the `.solve()` step, the second visualization has very different looking links...

bug
Priority:Low
flowsheet viewer
ui

This is a list of enhancements we can have for the double loop after #787 is merged. - [x] Abstraction on the bidding and tracking model objects: https://github.com/IDAES/idaes-pse/pull/787#discussion_r848854374 - [...

Priority:Low
discussion
DISPATCHES

For the pipeline models, I'd like to add a `pressure_dx` variable, and would like to use `ControlVolume1D`'s method for doing so. I do not, however, want a `deltaP` variable or...

help wanted
Priority:Low