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In the following pages, you will find a list of all the different types of errors that can occur while executing the component selection calculation step. The best method to find the specific error is through the search function.

• Authority smaller than minimal required authority

• KVS value et to zero

• Fixed pressure drop lower than required pressure drop

• Pump head not enough for pressure loss

• Total pressure drop larger than 20 bar

• No pumps provide pressure for this control valve

• Both pump head and pump curve are locked

• Design flow rate out of range of pump curve

• Heat exchanger supply/return temperatures too close together

• No suitable valve position can achieve desired mixing ratio

• Short circuit on premix by-pass

• ... has pump downstream

• No pumps expected

Did you hit an error and could not find an explainer for it, please let us know at support@hysopt.com.

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