Device for seperating gas from liquid

A gas-liquid separating apparatus capable of sufficiently separating gas in gas-liquid mixture fluid from liquid therein, is disclosed. Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus b...

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Hauptverfasser: YASUSHI MORI, NOBUHIRO HOKAO, TOKUJI MATSUO
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Sprache:eng
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creator YASUSHI MORI
NOBUHIRO HOKAO
TOKUJI MATSUO
description A gas-liquid separating apparatus capable of sufficiently separating gas in gas-liquid mixture fluid from liquid therein, is disclosed. Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus becomes a rotating flow 8 along the inner wall surface of the cylinder 9, and thereby centrifugal separation between gas and liquid is effected. The separated steam is discharged from a secondary separator 11 through a cap 18 into a gas-phase section within a drum 1. A part of the primary isolated water 8 of the rotating flow has its outflow velocity decelerated by a perforated plate 23, and thereafter flows out to a liquid-phase section within the drum 1. As a result, a flow velocity of the primary isolated water 20 flowing out through a primary isolated water outlet 17 to the liquid-phase section within the drum 1 is decreased as compared to the case where the prior art was employed, and hence, an amount of the primary isolated water drawn into a flow 22 within the drum is reduced. Moreover, since the primary isolated water 21 having flowed out through the perforated plate 23 to the liquid-phase section within the drum 1 has a slow outflow velocity, it becomes an upward blow in the vicinity of the cylinder 9 due to influence of a buoyancy acting upon a steam component. Accordingly, the time available for gravitational separation of gas and liquid in the liquid phase within the drum 1 can be reserved longer than in the case of employing the prior art.
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Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus becomes a rotating flow 8 along the inner wall surface of the cylinder 9, and thereby centrifugal separation between gas and liquid is effected. The separated steam is discharged from a secondary separator 11 through a cap 18 into a gas-phase section within a drum 1. A part of the primary isolated water 8 of the rotating flow has its outflow velocity decelerated by a perforated plate 23, and thereafter flows out to a liquid-phase section within the drum 1. As a result, a flow velocity of the primary isolated water 20 flowing out through a primary isolated water outlet 17 to the liquid-phase section within the drum 1 is decreased as compared to the case where the prior art was employed, and hence, an amount of the primary isolated water drawn into a flow 22 within the drum is reduced. Moreover, since the primary isolated water 21 having flowed out through the perforated plate 23 to the liquid-phase section within the drum 1 has a slow outflow velocity, it becomes an upward blow in the vicinity of the cylinder 9 due to influence of a buoyancy acting upon a steam component. 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Gas-liquid mixture fluid fed from a boiler evaporator tube enters through a separator inlet 15 into a cylinder 9 of a separator 12 in a tangential direction, thus becomes a rotating flow 8 along the inner wall surface of the cylinder 9, and thereby centrifugal separation between gas and liquid is effected. The separated steam is discharged from a secondary separator 11 through a cap 18 into a gas-phase section within a drum 1. A part of the primary isolated water 8 of the rotating flow has its outflow velocity decelerated by a perforated plate 23, and thereafter flows out to a liquid-phase section within the drum 1. As a result, a flow velocity of the primary isolated water 20 flowing out through a primary isolated water outlet 17 to the liquid-phase section within the drum 1 is decreased as compared to the case where the prior art was employed, and hence, an amount of the primary isolated water drawn into a flow 22 within the drum is reduced. Moreover, since the primary isolated water 21 having flowed out through the perforated plate 23 to the liquid-phase section within the drum 1 has a slow outflow velocity, it becomes an upward blow in the vicinity of the cylinder 9 due to influence of a buoyancy acting upon a steam component. Accordingly, the time available for gravitational separation of gas and liquid in the liquid phase within the drum 1 can be reserved longer than in the case of employing the prior art.</abstract><edition>5</edition><oa>free_for_read</oa></addata></record>
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subjects BLASTING
HEATING
LIGHTING
MECHANICAL ENGINEERING
METHODS OF STEAM GENERATION
PERFORMING OPERATIONS
PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
SEPARATION
STEAM BOILERS
STEAM GENERATION
TRANSPORTING
WEAPONS
title Device for seperating gas from liquid
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