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Water disengaging drum

Consideration of All Releases into the System - All releases tied into the closed system must be considered. In addition to PR valve discharges, these may include fuel gas compressor and absorber knockout drum drainage, vapors vented from water disengaging drums, feed diversion streams, closed drainage from equipment, vapor blowdowns and liquid pulldowns. [Pg.208]

With the flare tip and flare seal pressure drop and flare elevation fixed, the flare stack, headers and laterials are sized for the largest release, while not exceeding the maximum allowable operating pressure on the associated blowdown drums and water disengaging drums. These maximum allowable operating pressures are in turn determined by ... [Pg.209]

Routing of Flare Header through Process Areas - Flare headers in process areas should be routed to avoid locations of particularly high fire risk, such as over pumps, near furnaces, etc. The headers and subheaders should also be laid out and provided with isolating CSO valves and spectacle blinds, unless prohibited by local codes, such that it is not necessary for flare lines to remain in service in units which are shut down separately. Blowdown and water disengaging drums should be spaced from process areas. [Pg.209]

Vessels Containing Light Ends - Discharges should be sent to either a water disengaging drum, a sour water disengaging drum or a spent caustic disengaging drum, and accompanied by appropriate treatment methods. [Pg.223]

A typical water disengaging drum system is illustrated in Figure 5. The... [Pg.239]

A design pressure of 545 kPa, gage is normally specified for water disengaging drums. The water outlet system is designed to seal the drum and prevent entrainment of hydrocarbon or air into the sewer. Figure 5 indicates the normal layout incorporating a single loop seal. [Pg.241]

The design of these drums generally follows the same basis as that for water disengaging drums, except that a pump (with spare) is required to transfer the aqueous liquid imder level control to the appropriate receiving facilities. [Pg.243]

This chapter discusses some of the criteria for selecting, designing and spacing elevated, burning-pit, and multijet flares. The design of safety valve and flare headers was covered in an earlier chapter, as well as discussions concerning associated blowdown drums, water disengaging drums, etc. [Pg.246]

A flare seal drum may also be used as a sour water disengaging drum, if economically advantageous. In such cases, special care should be given to ensure that the drum is adequately sized to simultaneously meet all design features required for both functions. Also a separate source of makeup water must still be provided to ensure continuity of the seal. [Pg.272]

If HjS is continuously present in the flare gas or if the flare seal drum also functions as a sour water disengaging drum, then the effluent seal water must be routed to a sour water stripper, desalter, or other safe means of disposal. Withdrawal from the drum is by pump in place of the normal loop seal arrangement. Two pumps are provided one motor driven for normal use, and the other having a steam turbine drive with low pressure cut-in. The seal drum level is controlled by LIC with high and low alarm lights plus an independent high level alarm. [Pg.276]

Aqueous plant effluent and drawoff streams such as steam condensate, sour water, or spent caustic soda solution may require disposal to a disengaging drum. [Pg.242]

It is important to note that even if the blowdown is effective in disengaging liquid and vapor, further condensation could occur downstream especially if the vented vapor exits the drum at a temperature above ambient conditions. A proportion of such condensible materials in the blowdown drum vapor release may condense as a result of cooling in the flare header and contact with seal water, and then disengage in the flare seal drum while condensible vapors which are not condensed out at this stage may condense in the flare stack or its inlet line, thus creating the potential for hazardous fallout of burning liquid from the flare. Condensed hydrocarbon in the seal drum can be entrained out with the... [Pg.225]

The first vessel in the blowdown system is therefore an acid-hydrocarbon separator. This drum is provided with a pump to transfer disengaged acid to the spent acid tank. Disengaged liquid hydrocarbon is preferably pumped back to the process, or to slop storage or a regular non-condensible lowdown drum. The vented vapor stream from the acid-hydrocarbon separator is bubbled through a layer of caustic soda solution in a neutralizing drum and is then routed to the flare header. To avoid corrosion in the special acid blowdown system, no releases which may contain water or alkaline solutions are routed into it. [Pg.234]

Fig. 2. Flowsheet of a typical FCCU. 1, riser 2, disengager 3, FFB regenerator 4, catalyst cooler 5, main fractionator 6, LCO stripper 7, HCO drum 8, accumulator I, fresh feed II, recycle feed III, slurry oil IV, LCO V, catalytic naphtha VI, rich gas VII, air VIII, flue gas IX, steam X, water/steam mixture XI, water. Fig. 2. Flowsheet of a typical FCCU. 1, riser 2, disengager 3, FFB regenerator 4, catalyst cooler 5, main fractionator 6, LCO stripper 7, HCO drum 8, accumulator I, fresh feed II, recycle feed III, slurry oil IV, LCO V, catalytic naphtha VI, rich gas VII, air VIII, flue gas IX, steam X, water/steam mixture XI, water.
Fire 1.4. Steam boiler and furnace arrangements. [Steam, Babcock and Wilcox, Barberton, OH, 1972, pp. 3.14, 12.2 (Fig. 2), and 25.7 (Fig. 5)]. (a) Natural circulation of water in a two-drum boiler. Upper drum is for steam disengagement the lower one for accumulation and eventual blowdown of sediment, (b) A two-drum boiler. Preheat tubes along the Roor and walls are cormected to heaters that feed into the upper drum, (c) Cross section of a Stirling-type steam boiler with provisions for superheating, air preheating, and flue gas economizing for maximum production of 550,000 Ib/hr of steam at 1575 psia and 900°F. [Pg.10]

In a drum boiler, water is circulated at a rapid rate upward through the furnace tubes, in which it partially vaporizes. Upon reaching the drum, the liquid disengages the vapor and returns through relatively cool downcomers to the bottom of the furnace to begin another pass upward. The most characteristic feature of drum boilers is the difficulty of controlling the level of liquid in the steam drum. A feedforward-feedback system for its control was described briefly in Chap. 8. [Pg.244]


See other pages where Water disengaging drum is mentioned: [Pg.209]    [Pg.225]    [Pg.232]    [Pg.240]    [Pg.242]    [Pg.243]    [Pg.209]    [Pg.225]    [Pg.232]    [Pg.240]    [Pg.242]    [Pg.243]    [Pg.241]    [Pg.246]    [Pg.242]    [Pg.242]    [Pg.271]    [Pg.355]    [Pg.10]    [Pg.50]    [Pg.10]    [Pg.50]    [Pg.478]   
See also in sourсe #XX -- [ Pg.225 , Pg.239 ]




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