Applying the ASME codes : plant piping and pressure vessels, by Wingate, James A

By Wingate, James A

Folllowing the luck of his first publication relating to Hydraulics, Pipe circulate, commercial HVAC & application platforms, Mister Mech Mentor now bargains an all-new, easy-to-read number of chapters that includes ASME Piping & strain Vessel Code functions. Written in a pleasant sort, this publication presents the basic merits of guide by way of a private mentor who explains why and the way, whereas educating very likely harmful classes in physics and engineering layout. Spared the embarrassment of painful blunders, either early-career and skilled engineers will achieve functional wisdom from frank, colourful situations and learn how to clear up a number of mechanical difficulties, together with: Pipe tension & pressure Structural helps strain Vessels Jacketed Pipes Bellows-Type growth Joints strategy Piping

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Applying the ASME codes : plant piping and pressure vessels, Edition: 2nd

Folllowing the luck of his first booklet regarding Hydraulics, Pipe movement, business HVAC & application platforms, Mister Mech Mentor now bargains an all-new, easy-to-read choice of chapters that includes ASME Piping & strain Vessel Code purposes. Written in a pleasant kind, this publication presents the basic merits of guideline through a private mentor who explains why and the way, whereas instructing possibly risky classes in physics and engineering layout.

Extra info for Applying the ASME codes : plant piping and pressure vessels, Edition: 2nd

Sample text

Spring constants in both Schemes #1 and #2. But the loadings are changed from 739 lb cold and 803 lb hot per spring in Scheme #1 to 694 and 757 lb, respectively, in the optimized configuration. Pipe Reaction on Terminal Equipment Pipe Reaction on Terminal Equipment The Summary, Table 3-1, taken from the same section of the report, shows a vertical load of −1,105 lb (downward on the heat exchanger) at Node 5 for this support scheme, and a negligible 172 lb horizontal load there. The moments impressed on the H/X flange are also shown: 3,258 ft-lb.

Also in the stress program printout with header Pipe Stress: Example No. ) This is not an excessive load for industrial plant pipe rack framing steel (LOAD CASE NO. 3, THL + WT). • At Node 50, the spring constant for Scheme #1 was 1,200 lb/in. (Grinnell Figure 82 Size 13 spring hanger), and for Scheme #2 the spring constant and Grinnell unit size (13) remain the same. However, in Scheme #1 the cold-set and (hot) operating loads are 2,509 and 2,416 pounds, respectively. In Scheme #2, by requesting the program to optimize the springs, we find the loadings are changed to 3,171 and 3,076 lb, respectively.

But the loadings are changed from 739 lb cold and 803 lb hot per spring in Scheme #1 to 694 and 757 lb, respectively, in the optimized configuration. Pipe Reaction on Terminal Equipment Pipe Reaction on Terminal Equipment The Summary, Table 3-1, taken from the same section of the report, shows a vertical load of −1,105 lb (downward on the heat exchanger) at Node 5 for this support scheme, and a negligible 172 lb horizontal load there. The moments impressed on the H/X flange are also shown: 3,258 ft-lb.

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