Apparatus for treating gas

Patent metadata

Field	Value
Publication number	US-10814336-B2
Application number	US-201615552715-A
Country	US
Kind code	B2
Filing date	Jan 28, 2016
Priority date	Feb 23, 2015
Publication date	Oct 27, 2020
Grant date	Oct 27, 2020

Abstract

Known wet electrostatic precipitators are large and inefficient. The present invention enables the production of smaller, more efficient and long lasting wet electrostatic precipitators by the addition of a central bore in the inner electrode through which a first purge flow is passed and directed into the precipitator chamber, perpendicular to the direction of flow of the gas to be treated through the chamber to urge the particulate into the water curtain. A second, larger, cleaning purge flow is also provided to disturb the water curtain such that it cleans the inner electrode of any deposited particulate.

First claim

The invention claimed is:

1. A wet electrostatic precipitator for treating a gas stream, comprising:
an electrostatic chamber having an electrostatic chamber inlet through which the gas stream to be treated is conveyed into the electrostatic chamber and an electrostatic chamber outlet through which the treated gas stream is conveyed from the electrostatic chamber, an inner electrode and an outer electrode arranged to produce an electrostatically charged field therebetween when an electrical potential is applied between said inner and outer electrodes, a liquid inlet for conveying liquid into the electrostatic chamber for providing a liquid curtain over an inner surface of the outer electrode, such that particulates in the gas stream become electrically charged when passing through the field and are drawn towards the outer electrode, where the particulates are entrained by the liquid curtain and removed from the gas stream, wherein the inner electrode comprises a conduit through which a purge gas can be conveyed and said inner electrode further comprises at least one opening located towards the electrostatic chamber inlet and arranged to convey the purge gas from the conduit into the electrostatic chamber substantially laterally to the gas stream flowing through the electrostatic chamber; and
a control configured for controlling a flow of purge gas through the conduit of the inner electrode such that in a first condition the purge gas is conveyed through the conduit at a first flow rate to perform at least one of directing the gas stream towards the outer electrode and disrupting the gas stream, and in a second condition the purge gas is conveyed through the conduit at a second higher flow rate for dislodging deposits accumulated in a region of said at least one opening in the inner electrode; wherein the control is operatively connected to a sensor for sensing the deposits and when the deposits have exceed a predetermined amount the control is configured to activate the second condition.

2. The wet electrostatic precipitator as claimed in claim 1 , wherein said at least one opening is arranged to perform at least one of directing the gas stream towards the outer electrode and disrupting the gas stream.

3. The wet electrostatic precipitator as claimed in claim 1 , wherein the at least one opening comprises at least two openings for conveying purge gas into the electrostatic chamber in substantially opposing lateral directions.

4. The wet electrostatic precipitator as claimed in claim 1 , wherein the electrostatic chamber comprises a side passage containing an end portion of the inner electrode distal from said at least one opening.

5. The wet electrostatic precipitator as claimed in claim 4 , wherein the side passage comprises an inlet for conveying purge gas into the side passage for purging the end portion of the inner electrode.

6. The wet electrostatic precipitator as claimed in claim 1 , wherein the second higher flow rate is sufficient to perturb the liquid curtain such that liquid is urged against the deposits for removing said deposits.

7. The wet electrostatic precipitator as claimed in claim 1 , wherein the sensor senses one of: a change in the electrical potential between the inner and outer electrodes; and a change in a flow of the gas stream through the electrostatic chamber.

8. An abatement system comprising a wet electrostatic precipitator as claimed in claim 1 , further comprising a plasma burner causing heat, or chemical, reaction of the gas stream with a plasma flare generated by a plasma torch in a reactor chamber for receiving the gas stream, the reactor chamber located upstream of the precipitator and having an outlet in gas communication with the inlet of the electrostatic chamber for conveying gas which has been plasma treated to the precipitator for further treatment.

9. The abatement system as claimed in claim 8 , comprising a second conduit connecting the outlet of the reactor chamber to the inlet of the electrostatic chamber, the second conduit being shaped to contain, at least temporarily, liquid having formed the liquid curtain.

10. The abatement system as claimed in claim 9 , wherein the outlet of the reactor chamber comprises at least one spray nozzle for spraying a liquid into the reactor chamber for cooling the gas stream downstream of the plasma flare, the second conduit containing, at least temporarily, liquid which has been sprayed into the reactor chamber.

11. The abatement system as claimed in claim 8 , wherein the at least one plasma torch is orientated such that the gas stream flows through the reactor chamber downwardly, and the precipitator is orientated such that the gas stream flows through the precipitator upwardly.

12. The abatement system as claimed in claim 8 , wherein the system comprises a plurality of plasma torches each associated with a respective wet electrostatic precipitator.

Assignees

• Edwards Ltd

Inventors

• Voronin Sergey Alexandrovich
• Attwood Mark James
• Chambers Andrew Arthur
• Bidder John Leslie

Classifications

• Y02C20/30

  of perfluorocarbons [PFC], hydrofluorocarbons [HFC] or sulfur hexafluoride [SF6] · CPC title

• B03C2201/10

  Ionising electrode with two or more serrated ends or sides · CPC title

• B03C3/80 Primary

  by gas or solid particle blasting · CPC title

• B03C3/49

  tubular · CPC title

• B03C3/41

  Ionising-electrodes · CPC title