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Extra resources for Petroleum engineering handbook 1-Facilities and Construction Engineering
9 gives guidelines that can be used for sizing nozzles, where ρm is the bulk density and Vm the bulk velocity. In addition, the API RP14E4 on erosion velocity should be included. This relationship is also given by an inlet momentum criterion as ρmVm2 = C 2, where C is given as 100 for continuous service and 125 for intermittent service. The value of C can also vary with pipe material, solids loading, and service. See the chapter on Piping and Pipelines in this section of the Handbook. Vortex breakers are generally required on the liquid outlets.
13 shows liquid levels for different vessel diameters. Step 4. Calculate vessel height from Eq. 17. 4. 5 to 3 range. Step 5. Select a vessel size that satisfies gas capacity, water-drop removal, and liquid-retention time requirements. An 84-in. 4-ft separator satisfies the requirements, so you would round up to an 84-in. 5-ft vessel. Similarly, a 90-in. 5-ft separator would also be satisfactory. Nomenclature Ad = C = CD = d = dh = dm = dpp = D = Do = Fc = Fg = Fl = g = h = hc = hg = ho = hw = K = L = Leff = Lss = P = required demister area API RP14E erosion constant, (lbm/ft-sec2)1/2 drag coefficient (see Appendix A for calculation) vessel internal diameter, in.
It is often used for bulk separation in conjunction with well testing as shown. The Print Search Chapter 1 Home Chapter 3 Bookmarks Help III-38 Petroleum Engineering Handbook—Vol. III Fig. ). Fig. ). streams are temporarily separated, measured and analyzed, then recombined. With this arrangement, no level control is necessary because the levels are maintained by hydraulic balance. • Fig. 31: A multitube cyclone inline separator, which causes a wet gas flowstream to be divided between a number of cyclone tubes.
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