By Melody Beattie
Is an individual else's challenge your challenge? If, like such a lot of others, you've overpassed your personal existence within the drama of tending to a person else's, you can be codependent--and you could end up during this publication.
The therapeutic touchstone of hundreds of thousands, this contemporary vintage through certainly one of America's best-loved and such a lot inspirational authors holds the main to realizing codependency and to unlocking its stultifying carry in your existence.
With instructive lifestyles tales, own reflections, workouts, and self-tests, Codependent No More is an easy, uncomplicated, readable map of the puzzling global of codependency--charting the trail to freedom and a life of therapeutic, desire, and happiness.
Melody Beattie is the writer of Beyond Codependency, The Language of Letting Go, Stop Being suggest to Yourself, and Playing It through Heart.
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Additional resources for Codependent No More: How to Stop Controlling Others and Start Caring for Yourself
The inlet tips of the impeller blades are generally at or near this location. ϭ exit of diffuser or the discharge flange or port of the pump (d). ϭ the direction of the flow. ϭ hub. ϭ inner limit of region or gap (Tables 4 and 5) ϭ ideal. ϭ impeller. ϭ pump inlet flange or port. ϭ inlet passage; that is, the passage from the pump inlet flange or port to the impeller. ϭ input to fluid. ϭ losses. ϭ “mechanical” (pertaining to efficiency, Eq. 9). ϭ component of velocity in the meridional plane (that is, the axialradial plane containing the axis of rotation).
N in cs) ϭ (m in cp)/sp. gr. r ϭ fluid mass density, lbf-sec2/ft4 (kg/m3),ϭ g/g. s ϭ solidity (Eq. 53). s ϭ Thoma’s cavitation parameter ϭ hsv/H. T or T or M ϭ torque, lbf-ft (N-m). f ϭ flow coefficient. fe ϭ Ve/Ue ϭ impeller inlet or eye flow coefficient. fi (or fi, 2) ϭ impeller exit flow coefficient ϭ Vm, 2/U2 (Figure 12). c ϭ head coefficient (Figure 12); stream function (Figure 14). ci ϭ ideal head coefficient [ϭ ci, 2 ϭ Vu, 2/U2 for zero inlet swirl (Vu, 1 ϭ 0)]. ci, 2 ϭ Vu, 2/U2 [ϭ ci for zero inlet swirl (Vu, 1 ϭ 0)].
P ϭ pressure rise, lbf/ft2 (Pa). pL ϭ pressure loss, lbf/ft2 (Pa). pL, i ϭ impeller pressure loss from its inlet to the point of interest, lbf/ft2 (Pa). pL, i ϩ I/L ϭ pressure loss pL, i in impeller plus pressure loss in inlet passage, lbf/ft2 (Pa). gpL ϭ all losses in the main flow passages from pump inlet to pump outlet, lbf/ft2 (Pa). pv or pvp ϭ vapor pressure of liquid being pumped, lbf/ft2 (Pa). PI ϭ power delivered to all fluid flowing through the impeller, ft-lbf/sec (kW). PS ϭ shaft power, ft-lbf/sec (kW).