From 9c7a0d1d680f5a2ce9492565fba1eebccdc4ed69 Mon Sep 17 00:00:00 2001 From: eprade Date: Thu, 7 Nov 2024 13:10:54 +0100 Subject: [PATCH] -updated changelog --- CHANGELOG.rst | 4 +++- 1 file changed, 3 insertions(+), 1 deletion(-) diff --git a/CHANGELOG.rst b/CHANGELOG.rst index 14fbb72c..06f12752 100644 --- a/CHANGELOG.rst +++ b/CHANGELOG.rst @@ -1,7 +1,7 @@ Change Log ============= -[0.11.0] - 2024-10-24 +[0.11.0] - 2024-11-07 ------------------------------- - [ADDED] heat_consumer component - [ADDED] heat_consumer plotting @@ -15,12 +15,14 @@ Change Log - [CHANGED] variable "alpha_w_per_m2k" to "u_w_per_m2k" - [CHANGED] option "all" for pipeflow heat calculations to "sequential", the new option is "bidirectional" - [CHANGED] volume flow in result tables instead of normalized volume flow for non gas fluids +- [CHANGED] introduction of slack mass flow into nodes as solved variable + circulation pumps are now branches and thus cannot generate or consume mass - [FIXED] Pressure plot not working for circ pump - [FIXED] volume flow rate for incompressible fluids based on real density, thus in this case results are renamed from "vdot_norm_m3_per_s" to "vdot_m3_per_s" - [FIXED] some imports from pandapower - [FIXED] NAN to nan because of numpy changes - [FIXED] if velocity in a branch is negative to get corrected nodes from the branch pit - [FIXED] plot pressure profile not working for circulation pump sources +- [FIXED] Infeed switches are considered correctly + Heat consumers with qext_w = 0 and temperature control ignore temperature set points + alpha also applied to mdot - [REMOVED] support for Python 3.8 due to EOL