An air cooled steam condenser having heat exchanger panels supported in a heat exchange frame section. A bottom bonnet runs along the bottom length of each heat exchanger panel for delivering steam to the bottom end of condenser tubes in the heat exchange panel and for receiving condensate formed in those same tubes. The tops of the tubes are connected to a top bonnet. Uncondensed steam and non-condensables are drawn into the top bonnet from the condenser tubes. A steam distribution manifold is located below the heat exchange section perpendicular to the longitudinal axis of the heat exchange panels and delivers steam to each heat exchange panel via a single steam inlet located at a center point of each bottom bonnet.

A process for extracting a condensable vapor from a supplied gas, comprising the steps of: i) condensing the condensable vapor by cooling the supplied gas at a condensing surface, such that the supplied gas is divided into at least one condensed fraction and a product gas; while ii) removing the at least one condensed fraction from the condensing surface by mechanical scraping means.

A process for extracting a condensable vapor from a supplied gas, comprising the steps of: i) condensing the condensable vapor by cooling the supplied gas at a condensing surface, such that the supplied gas is divided into at least one condensed fraction and a product gas; while ii) removing the at least one condensed fraction from the condensing surface by mechanical scraping means.

Large scale field erected air cooled industrial steam condenser having 10 heat exchanger bundles per cell arranged in five pairs in a V-shape, each heat exchanger bundle having four primary heat exchangers and four secondary heat exchangers in which each secondary heat exchanger is paired with a single primary heat exchanger. Four primary condensers are arranged such that the tubes are horizontal, while the inlet steam manifolds at one end of the tubes are perpendicular to the primary condenser tubes, i.e., parallel to the transverse axis of the bundle. Steam enters the small inlet steam manifolds from below. Cross-sectional dimensions of the tubes are 200 mm wide with a cross-section height of less than 10 mm with fins that are 10 mm in height, arranged at 9 to 12 fins per inch.

Large scale field erected air cooled industrial steam condenser having 10 heat exchanger bundles per cell arranged in five pairs in a V-shape, each heat exchanger bundle having four primary heat exchangers and four secondary heat exchangers in which each secondary heat exchanger is paired with a single primary heat exchanger. Four primary condensers are arranged such that the tubes are horizontal, while the inlet steam manifolds at one end of the tubes are perpendicular to the primary condenser tubes, i.e., parallel to the transverse axis of the bundle. Steam enters the small inlet steam manifolds from below. Cross-sectional dimensions of the tubes are 200 mm wide with a cross-section height of less than 10 mm with fins that are 10 mm in height, arranged at 9 to 12 fins per inch.

Modular air cooled condenser apparatus and related methods are disclosed. An example mechanical draft modular air cooled condenser disclosed herein includes an example condenser module that includes a plenum and a first condenser bundle having a first set of tubes having first ends and second ends and a first condensate header connected to the second ends of the tubes. The example condenser module also includes a second condenser bundle having a second set of tubes having third ends and fourth ends and a second condensate header connected to the fourth ends of the second set of tubes. In addition, the condenser module includes a third condenser bundle having a third set of tubes having fifth ends and sixth ends and a third condensate header connected to the sixth ends of the third set of tubes. The condenser module also includes a fourth condenser bundle having a fourth set of tubes having seventh ends and eighth ends and a fourth condensate header connected to the eighth ends of the fourth set of tubes. The condenser module further includes a shroud that houses a single fan, the single fan positioned to create a draft to flow over the first condenser bundle, over the second condenser bundle, over the third condenser bundle, and over the fourth condenser bundle. In addition, the condenser module includer a support frame that supports the first, second, third, and fourth condenser bundles.

Modular air cooled condenser apparatus and related methods are disclosed. An example mechanical draft modular air cooled condenser disclosed herein includes an example condenser module that includes a plenum and a first condenser bundle having a first set of tubes having first ends and second ends and a first condensate header connected to the second ends of the tubes. The example condenser module also includes a second condenser bundle having a second set of tubes having third ends and fourth ends and a second condensate header connected to the fourth ends of the second set of tubes. In addition, the condenser module includes a third condenser bundle having a third set of tubes having fifth ends and sixth ends and a third condensate header connected to the sixth ends of the third set of tubes. The condenser module also includes a fourth condenser bundle having a fourth set of tubes having seventh ends and eighth ends and a fourth condensate header connected to the eighth ends of the fourth set of tubes. The condenser module further includes a shroud that houses a single fan, the single fan positioned to create a draft to flow over the first condenser bundle, over the second condenser bundle, over the third condenser bundle, and over the fourth condenser bundle. In addition, the condenser module includer a support frame that supports the first, second, third, and fourth condenser bundles.

A power plant includes a power generating system, a tower housing and an evaporative cooling system which includes at least one multiple-effect evaporative condenser. The multiple-effect evaporative condenser includes a pumping device, a first cooling unit and a second cooling unit. The first cooling unit includes a first water collection basin for collecting said cooling water from the pumping device, a plurality of first heat exchanging pipes connected to the condenser and immersed in the first water collection basin, and a first fill material unit provided underneath the first heat exchanging pipes. The second cooling unit includes a second water collection basin positioned underneath the first cooling unit for collecting said cooling water flowing from the first cooling unit, a plurality of second heat exchanging pipes immersed in the second water collection basin, and a second fill material unit provided underneath the second heat exchanging pipes.

A power plant includes a power generating system, a tower housing and an evaporative cooling system which includes at least one multiple-effect evaporative condenser. The multiple-effect evaporative condenser includes a pumping device, a first cooling unit and a second cooling unit. The first cooling unit includes a first water collection basin for collecting said cooling water from the pumping device, a plurality of first heat exchanging pipes connected to the condenser and immersed in the first water collection basin, and a first fill material unit provided underneath the first heat exchanging pipes. The second cooling unit includes a second water collection basin positioned underneath the first cooling unit for collecting said cooling water flowing from the first cooling unit, a plurality of second heat exchanging pipes immersed in the second water collection basin, and a second fill material unit provided underneath the second heat exchanging pipes.

Large scale field erected air cooled industrial steam condenser having 10 heat exchanger bundles per cell arranged in five pairs in a V-shape, each heat exchanger bundle having four primary heat exchangers and four secondary heat exchangers in which each secondary heat exchanger is paired with a single primary heat exchanger. Four primary condensers are arranged such that the tubes are horizontal, while the inlet steam manifolds at one end of the tubes are perpendicular to the primary condenser tubes, i.e., parallel to the transverse axis of the bundle. Steam enters the small inlet steam manifolds from below. Cross-sectional dimensions of the tubes are 200 mm wide with a cross-section height of less than 10 mm with fins that are 10 mm in height, arranged at 9 to 12 fins per inch.