Low pressure drop static mixing system
AssigneeADA-ES, Inc.
InventorRonald Hanson
Life of this patent
Estimating the term…
Abstract
A contaminated gas stream can be passed through an in-line mixing device, positioned in a duct containing the contaminated gas stream, to form a turbulent contaminated gas stream. One or more of the following is true: (a) a width of the in-line mixing device is no more than about 75% of a width of the duct at the position of the in-line mixing device; (b) a height of the in-line mixing device is no more than about 75% of a height of the duct at the position of the in-line mixing device; and (c) a cross-sectional area of the mixing device normal to a direction of gas flow is no more than about 75% of a cross-sectional area of the duct at the position of the in-line mixing device. An additive can be introduced into the contaminated gas stream to cause the removal of the contaminant by a particulate control device.
Claims25
A method, comprising:
- receiving a contaminated gas stream comprising a contaminant;
- passing the contaminated gas stream through an in-line mixing device, positioned in a duct containing the contaminated gas stream, to form a turbulent contaminated gas stream;
- introducing an additive to the contaminated gas stream, the additive at least partially removing or causing the removal of the contaminant;
- and
- thereafter removing, by a particulate control device, particulates from the additive-containing contaminated gas stream, wherein the particulates comprise at least some of the contaminant and/or a derivative thereof,
- wherein the in-line mixing device comprises a static mixing device comprising one or more stationary mixing elements fixed in a housing of the static mixing device, wherein the static mixing device is attached to a mechanical system that rotates the static mixing device relative to a flow direction of the contaminated gas stream, wherein, when in a first position relative to the flow direction, the contaminated gas stream has a first pressure drop over the in-line mixing device, wherein, when in a different second position relative to the flow direction, the contaminated gas stream has a second pressure drop over the in-line mixing device, wherein the first and second pressure drops are different, and
- wherein at least one of the following is true;
- (a) a width of the in-line mixing device is no more than about 75% of a width of the duct at the first position of the in-line mixing device;
- (b) a height of the in-line mixing device is no more than about 75% of a height of the duct at the first position of the in-line mixing device;
- and
- (c) a cross-sectional area of the in-line mixing device normal to a direction of gas flow is no more than about 75% of a cross-sectional area of the duct at the first position of the in-line mixing device.
A method, comprising:
- receiving a contaminated gas stream comprising a contaminant;
- introducing an additive into the contaminated gas stream, the additive at least partially removing or causing the removal of the contaminant
- passing the additive-containing contaminated gas stream through an in-line mixing device, positioned in a duct containing the additive-containing contaminated gas stream, to form a turbulent contaminated gas stream, wherein, in a first operating mode, the in-line mixing device has a first position relative to a direction of flow of the additive-containing contaminated gas stream and, in a second operating mode, the in-line mixing device has a different second position relative to the direction of flow of the additive-containing contaminated gas stream and wherein one or more of the following is true:
- (a) the first operating mode provides a first pressure drop of the additive-containing contaminated gas stream passing the in-line mixing device and the second operating mode provides a second pressure drop of the additive-containing contaminated gas stream passing the in-line mixing device, the first pressure drop being greater than the second pressure drop;
- (b) the first operating mode provides a first level of turbulent flow of the additive-containing contaminated gas stream passing the in-line mixing device and the second operating mode provides a second level of turbulent flow of the additive-containing contaminated gas stream passing the in-line mixing device, the first level of turbulent flow being greater than the second level of turbulent flow;
- (c) in the first operating mode, a plane of a face of the in-line mixing device has a first angular orientation relative to a direction of flow of the additive-containing contaminated gas stream and in the second operating mode the plane of the face of the in-line mixing device has a second angular orientation relative to the direction of flow of the additive-containing contaminated gas stream, the first and second angular orientations being different;
- and
- (d) in the first operating mode and during a selected time interval, a first amount of the additive-containing contaminated gas stream passes through the in-line mixing device and, in the second operating mode and during the selected time interval, a second amount of the additive-containing contaminated gas stream passes through the in-line mixing device, the first amount being greater than the second amount;
- and
- thereafter removing, by a particulate control device, particulates from the additive-containing contaminated gas stream, wherein the particulates comprise at least some of the contaminant and/or a derivative thereof.
A method, comprising:
- receiving a contaminated gas stream comprising a contaminant;
- introducing an additive into the contaminated gas stream, the additive at least partially removing or causing the removal of the contaminant;
- determining, by a computer, a desired flow resistance and/or pressure drop across an in-line mixing device positioned in the contaminated gas stream to distribute the additive throughout the contaminated gas stream;
- determining, by the computer, a desired orientation of the in-line mixing device and/or a mixing element thereof relative to a flow path of the contaminated gas stream to produce the desired flow resistance and/or pressure drop across the in-line mixing device;
- determining, by the computer, a current orientation of the in-line mixing device and/or a mixing element thereof relative to a flow path of the contaminated gas stream, wherein the current and desired orientations are different;
- causing, by the computer, the in-line mixing device to change from the current orientation to the desired orientation;
- and
- removing, by a particulate control device, particulates from the contaminated gas stream, wherein the particulates comprise at least some of the contaminant and/or a derivative thereof.
Dependencies are inferred from the claim text.