A regenerative thermal oxidizer (RTO) with three or more chambers. Each chamber would be in a unique mode, (inlet, outlet, purge). Each chamber has its gas flow determined by two poppet valves which define which mode the chamber will be in: inlet mode, output mode, or purge mode.

A regenerative thermal oxidizer (RTO) with three or more chambers. Each chamber would be in a unique mode, (inlet, outlet, purge). Each chamber has its gas flow determined by two poppet valves which define which mode the chamber will be in: inlet mode, output mode, or purge mode.

A dedicated outdoor air system and method that is capable of operating over a broader spectrum of conditions. The HVAC system of the present invention utilizes a heating means positioned within the return air passageway in order to optimize the regeneration of the desiccant wheel and energy recovery device. By positioning a heating means upstream of the regeneration side of the desiccant wheel, the system is capable of providing supply air having low dew points to the enclosed space while still providing improved energy efficiency over conventional HVAC systems.

The disclosure relates to a heat transfer assembly for a rotary regenerative heat exchanger. The assembly includes a rotor arranged between at least two separated fluid flow passages passing flow axially through the rotor, where each flow passage is connected to a sector part of the rotor. The assembly further includes a plurality of channels in the rotor for flowing a fluid through the rotor, each of the channels is enclosed by heat transfer and heat accumulating surfaces in the rotor, and the heat transfer and heat accumulating surfaces of the channels are made in a material providing an average axial thermal conductivity less than 100 W/mK arranged to reduce the Longitudinal Heat Conductivity of the rotor.

A method for producing a sector plate for a rotary heat exchanger is disclosed. The method includes defining overall dimensions of a sector plate. A number of a plurality of tapered ribs to be included on the top surface is determined based on a surface area of the sector plate and/or a sealing to be provided by the sector plate. Additionally, a root height of the plurality of tapered ribs is determined based on at least a plate thickness of the sector plate and the number of the plurality of tapered ribs. With the root height, the plurality of tapered ribs cause the sector plate to deform parabolically in response to an actuation. The plurality of tapered ribs also return the sector plate to a rest position and the sector plate supports its weight in a cantilevered fashion when in the actuated position and the rest position.

A rotary heat exchanger includes: a tubular-shaped heat transfer tubular body (3) which is rotatable with a central axis (C) as a rotation center, which allows a first medium (11) to flow therein, and outside of which a second medium (12) having a temperature different from a temperature of the first medium (11) flows; a central member (2) which is provided on an inner side of the heat transfer tubular body (3) in a radial direction and which is fixed coaxially with the heat transfer tubular body (3); and an outer sliding contact member (6) which is in sliding contact with an outer circumferential surface of the heat transfer tubular body (3), and the heat transfer tubular body (3) is rotatably supported with respect to the central member (2) via bearings (17, 18) disposed at two end portions of the central member (2) in an axial direction.

A rotary heat exchanger includes: a tubular-shaped heat transfer tubular body (3) which is rotatable with a central axis (C) as a rotation center, which allows a first medium (11) to flow therein, and outside of which a second medium (12) having a temperature different from a temperature of the first medium (11) flows; a central member (2) which is provided on an inner side of the heat transfer tubular body (3) in a radial direction and which is fixed coaxially with the heat transfer tubular body (3); and an outer sliding contact member (6) which is in sliding contact with an outer circumferential surface of the heat transfer tubular body (3), and the heat transfer tubular body (3) is rotatably supported with respect to the central member (2) via bearings (17, 18) disposed at two end portions of the central member (2) in an axial direction.

The leakage reduction system includes a heat exchanger, a duct arrangement and a separation arrangement. The heat exchanger includes a rotor assembly rotatably mounted along a rotor post. The heat exchanger further includes a second inlet plenum, whereat the duct arrangement is configured. Further, the separation arrangement is incorporated at the duct arrangement dividing thereto into primary and secondary inlets. Through the primary inlet, a flue gas enriched with Oxygen is carried, and through the secondary inlet a recycled flue gas flow is allowed to be carried, keeping the Oxygen enriched recycled flue gas flow substantially away from turnover towards the flue gas flow to avoid turnover towards a flue gas flow, reducing leakage thereof.

Disclosed herein is a heat exchanger for transferring heat between a first gas flow and a second gas flow, the heat exchanger comprising at least two sectors; a first sector that is operative to receive a combustion air stream; and a second sector that is opposed to the first sector and that is operative to receive either a reducer gas stream or an oxidizer gas stream, and a pressurized layer disposed between the first sector and the second sector; where the pressurized layer is at a higher pressure than combustion air stream, the reducer gas stream and the oxidizer gas stream.

Disclosed herein is a heat exchanger for transferring heat between a first gas flow and a second gas flow, the heat exchanger comprising at least two sectors; a first sector that is operative to receive a combustion air stream; and a second sector that is opposed to the first sector and that is operative to receive either a reducer gas stream or an oxidizer gas stream, and a pressurized layer disposed between the first sector and the second sector; where the pressurized layer is at a higher pressure than combustion air stream, the reducer gas stream and the oxidizer gas stream.