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Sample text

Vertical Vessels. The seam-to-seam length of the vessel should be determined from the geometry, once a diameter and height of liquid volume are known. Allowance must be made for the inlet nozzle, space above the liquid level, gas separation section, mist extractor, and for Print Search Chapter 1 Home Chapter 3 Bookmarks Help III-48 Petroleum Engineering Handbook—Vol. III Fig. ). any space below the water outlet as shown in Fig. 31. For screening purposes, the following approximations can be used, where d is the vessel diameter).

The weight of the paraffin causes it to slough off of the coated surface before it builds up to a harmful thickness. In general, paraffinic oils are not a problem when the operating temperature is above the cloud point (temperature at which paraffin crystals begin to form). The problems arise, however, during a shutdown, when the oil has a chance to cool. Paraffin comes out of solution and plates surfaces. When production is restored, the incoming fluid may not be able to flow to the plated areas to dissolve the paraffin.

Given Values. 8 lbm / ft3 Operating pressure 1,000 psia Operating temperature 60 ° F Liquid-retention time 10 minutes each phase Inlet nozzle 12 in. Drop removal from gas 100 μm Water density Step 1. Calculate vessel diameter based on gas capacity from Eq. 9. d 2 = 5,054 TZQ g P (| ρg ρl − ρ g |) CD 1/2 dm . 0337................................................ 35 . 8 in . 26) Step 2. Calculate the vessel diameter based on water drop removal from Eq. 11 for a 500μm drop. 270 × 5002 = 4,936...............................

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