If the amount of flash steam is large, the design becomes almost identical to that of steam piping.
As the specific volume of steam is 100’s to over 1,000 times that of condensate, condensate return piping is more like steam piping than water piping.
The other end of the emergency residual heat discharging cooler (13) is connected to a steam pipeline joint (17).
The invention relates to a steam power plant (1) having a bypass pipeline (12) which connects the fresh steam line (5) flow to the exhaust steam line (6), wherein a bypass steam desuperheater (20) is disposed in the bypass pipeline (12).
The latter (4) has a steam conduit (5), which connects the container to an iron (6) and is attached to the pressurised-steam container (4) by means of a steam-conduit connection (8).
Preferably, the water suction conduit (8) is connected with the steam conduit (3) in such a manner that the flow of steam through the steam conduit (3) sucks water and/or air out of the water suction conduit (8).
The superheated steam line is split into a return line (33) leading to a heat exchange line (35) through the steam drum, and a header feed line (34).
steam-line rupture accident
The bypass line (Lc) converges (B1) with a vapor line for interconnecting a dry container (1) and the suction side of the vapor compressor (2).
A steam line (27, 22) directs the steam of increased pressure from the steam jet ejector (24) to the CO2 capture plant (10).
The invention relates to an exhaust steam line for steam plants comprising several, particularly air-cooled condensation elements.
A steam conduit (75) also extends within the housing (24, 25) for delivering steam from the steam chamber (26) to the condenser (27).
The valve assembly (12) is operatively disposed along the vapor line (28) or the recirculation line (26).
Isolation valves are located outside the containment structure on a feedwater line, the steam line, and the condensate injection line.
A bypass vapor path (22) bypassing the vapor compressor is provided in the vapor duct (19), and an open/close valve (23) is provided in the bypass vapor path.
A vapor line (28) is configured to fluidly extend between the fuel tank (14) and the vapor canister (18).
The cross section of the main steam line (10) becomes smaller from a connection point (7) of a bifurcating line (6).
Steam-volatile abhesive agents are preferred and are metered into the steam moistening process via the steam line.
Requêtes fréquentes français :1-200, -1k, -2k, -3k, -4k, -5k, -7k, -10k, -20k, -40k, -100k, -200k, -500k, -1000k,
Requêtes fréquentes anglais :1-200, -1k, -2k, -3k, -4k, -5k, -7k, -10k, -20k, -40k, -100k, -200k, -500k, -1000k,
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