Patent Grant
10449554
Electrostatic filter with electrical resistors and with a collector of solid or liquid particles, which changes according to the application, which removes the solid and/or liquid particles from a gaseous medium, and which is applied in the industrial sector, mainly in the industry of hydrocarbons at the stages of production, process, transport and distribution of gases.
Nowadays, the electrostatic filter exists, which is used in industrial applications for the filtering of gases in temperatures ranging from 15° C. to 200° C., consisting of a certain number of separated circular tubes or shared-walled polygonal tubes; in the center of which, either the circular tube or the polygonal one, there is an electrode subjected to a certain electric voltage normally between 30 kV and 50 kV, which causes a potential difference that decreases along the radius and becomes zero on the inner wall of the tube called collector, since it is electrically grounded. The number of tubes depends on the amount of gas, thus they become numerous (from 50 to 100 tubes normally) and their diameter is about 170 millimeters. The high voltage at the electrode creates a corona effect on gas, ionizing it due to the strong impact of the electrons against the gaseous molecules, an effect that occurs in neighboring regions along the electrode. In a little more distant regions, the little less accelerated electrons adhere to large surfaces, microscopically speaking, as they are particles of solid or liquid nature, thus charging them negatively. These charged particles are driven radially by the field towards the collector. The particles or dirt close to the inner wall of the tube descend because the drag force in this zone is minimal due to the laminar flow of the gas. The collection is obtained in the lower part of the tube where there is a chamber from which the tubes are born and that serves for the distribution of the gas incoming to all the tubes that are set parallelly. The gas is collected through an upper chamber which all the tubes share, it then passes on to the subsequent process.
The fact of having several tubes in parallel and that the tubes in parallel do not offer a considerable loss of pressure causes the gas to take preferential paths, thus resulting in higher flows in some tubes where the residence time of the gas will be much lower than the calculated. Thus the filtering efficiency, which is understood as the amount of particles of certain size filtered contrasted with the total amount of that size, is affected tremendously.
As the gas flow is smaller than that of the design, the above-mentioned effect will be boosted, increasing so the likelihood that the entire gas flow passes only through one tube, wherewith efficiency will be much lower than expected; therefore the outgoing gas will carry the majority of unwanted liquid or solid particles.
As collecting surface mainly made of stainless steel, only the internal walls of the tubes are used, thus requiring a large amount of steel, making the electrostatic filter one of the most expensive filtering technologies available in the industry.
Due to the arrangement and geometry of the electrode, just one side is tied, and usually on the higher side. Being the electrode larger than one meter and of fine diameter; to maintain the verticality becomes impossible and wherever the electrode is tilted, the emission of electrons is specially favored on the side closer to the wall of the collector tube. Considering that the amount of electrons emitted by the high voltage module is constant and limited at a certain maximum amount for which it was designed; due to the mentioned lack of verticality, a non-uniform distribution of a limited quantity of electrons occurs, being therefore the emitted quantity of electrons not the same neither along the electrode nor in all the filter tubes, fact that reduces tremendously the efficiency of the filter. Monitoring of the verticality of the electrode is done mostly visually from above (which might cause a perspective error). Due to the long time this task demands, it is costly and might cause long production shut downs.
For gases with a dew point temperature greater than the environment temperature, there will be condensation along the inner wall of tubes, due to their large heat exchange surface. Producing unwanted condensate that could chemically stick or adhere itself to the walls; thus obstructing the tube gradually in certain parts, which would cause electrical grounded zones or even points closer to the electrode, incurring the problem mentioned in the previous item.
For gases produced from high temperature reactors ranging from 300° C. to 900° C., where soot particular reactions carries on, it is normally desired to filter the soot or micron dust leaving the reactor, it is impossible to use the current configuration for the effect mentioned in the previous item. Additionally, the soot or micron dust would be added to the condensate in the walls forming a paste that would not descend, blocking the filter almost immediately.
In order to filter gases at high temperature, the ceramic filter is the best option nowadays but has a larger pressure drop (high energy consumption) and frequent clogging, increasing so, maintenance period and cost.
The invention is an electrostatic filter which allows the filtration of solid and liquid particles in gases. It consists of a case (3), preferably cylindrical, with a filter inlet (14) through which the gas enters tangentially to the inner wall and subsequently leaves the filter through the insulated outlet (5) attached to the top of the distributor disc (8) and ends in the filter cap (1). The insulated outlet (5) is located in the central part of the filter cap (1) which is electrically insulated from the distributor disc despite contact. The bottom side of the distributor disc (8) is attached to several concentric diffusers (10), preferably cylindrical, which host along their inner and outer walls the electrodes (2), which are several rods of very thin diameter that contact at top the distributor disc (8) and are spaced equidistantly from one another. The distributor disc (8) is supported by the filter cap (1) through junction elements or pins between the insulated supports (7) and the disc connectors (16) through which the electric voltage is communicated to the distributor disc (8) thanks to an external insulated high-voltage electric conductor (11) inserted through the internal hole of the insulated supports (7) that contacts the head of the disc connectors (16).
The case (3) is attached to the main collector (9) preferably conical with small slots (18) for liquid particle filtering applications, and with large and widely open slots for solid particle filtering applications. The main collector (9) is at zero or ground voltage and supports internally the concentric collectors (15), preferably cylindrical, equally spaced between them and the concentric diffusers (10). The space between the concentric collectors (15) and the main collector (9) at the startup, starts filled with solid or liquid particles up to a certain level which is slightly higher than the upper edge of the slots of the concentric collectors (15) and level remains constant thanks to the discharge star valve (6) referenced to a certain level by means of a level sensor not shown.
The case (3), is attached to the filter cap (1) through anchoring bolts, and externally contacts the internal face of electrical resistors (4) that surround it and heat it when needed, to keep filter temperature, measured by the thermocouples (12), as desired. The filter is covered by a thermal insulator (17) to avoid heat exchange with the environment.
Due to the filter configuration, explained in the previous paragraphs, it is achieved that the gas enters tangentially and then descends producing a cyclonic effect until a certain elevation, obtaining later a ring shaped profile of descent between the inner wall of the case (3) and the outer wall of the first concentric diffuser (10) where the charge and the expulsion of the particles to the concentric collectors happens. The gas then rises through the concentric ring between the inner wall of the first of the concentric diffusers (10) and the outer wall of the first of the concentric collectors (15) and the same happens for the next of the concentric diffusers and concentric collectors, following an upward and downward trajectory being subjected to the effect of electrostatic precipitation until reaching the insulated outlet (5). The solid and liquid particles precipitate down to the main collector (9).
After entering, the gas descends for a sufficient time as to uniform and occupy all the space between the concentric diffusers (10) and the concentric collectors (15), thus ensuring that the gas flow passes through the entire filtering field; not reducing efficiency.
In the case that the flow is lower than that of the design, the gas will have a longer residence time, being this more advantageous, because the charged particle will be more likely to reach the concentric collectors (15) before leaving the filter.
As collecting surface, the inner surface of the case (3) is used, plus the inner and outer surfaces of the concentric collectors (15), thus optimizing the material used and the volume of the filter too.
The verticality of the electrodes (2) is ensured by the verticality of the concentric diffusers (10), thus achieving a uniform controlled electrons rain along the electrodes (2) and thereby along the single trajectory of the gas.
The temperature of the filter is controlled by the electrical resistors (4) at a desired value higher than the dew point of the gas avoiding therefore unwanted condensable elements; incrustations and adhesions.
For gases produced by high temperature reactors; the filter can be brought to a temperature higher than gas dew point, thus obtaining a dry filtration of the micron particles produced contained in the gas stream as soot for instance.
The configuration of the filter allows easily the lifting of the internal parts, right after the filter cap (1) has been unmounted, making a quick and non-contact maintenance. It only requires pressurized water on the concentric diffusers (10) and collectors (15).
Maintenance is low since configuration avoids the accumulation of solid or liquid due to their evacuation by the star valve (6)
| Number | Date | Country | Kind |
|---|---|---|---|
| 000294-2015/DIN | Mar 2015 | PE | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/PE2016/000002 | 2/29/2016 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2016/140583 | 9/9/2016 | WO | A |
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| 20130133518 | Allan | May 2013 | A1 |
| Number | Date | Country | |
|---|---|---|---|
| 20180029043 A1 | Feb 2018 | US |
