System, method, and apparatus for ameliorating deposits in selective catalytic reduction systems for the reduction of nitrogen oxide emissions in steam methane reformers
A system, method, and apparatus for ameliorating deposits in selective catalytic reduction systems for the reduction of nitrogen oxide emissions in steam methane reformers. The system includes positioning a dual stage refractory particulate (RP) filter placed in an upstream airflow from a Selective Catalytic Reduction System (SCRS). The first stage is formed of a perforated steel plate with a second stage formed of a wire mesh screen. The system may employ air cannons to clean each of the first stage and the second stages.
1. An apparatus for reducing particulate blockage of a catalyst bed in a coal fired refractory, comprising:
a dual element screen having a first stage and a second stage disposed within a frame at a desired separation distance between the first stage and the second stage;
the first stage formed as a perforated steel plate having a plurality of apertures defined through a thickness of the perforated steel plate, the plurality of apertures defined in a spaced apart relation throughout a surface of the first stage, the perforated steel plate having a first open area ratio (OAR) between the plurality of apertures and a surface of the perforated steel plate of at least 30%; and
the second stage formed as a wire mesh screen having a second OAR between a pore and a surface area of the wire mesh screen of at least 30%.
2. The apparatus of claim 1 , wherein the first OAR is between 30% and 80%.
3. The apparatus of claim 2 , wherein the second OAR is between 30% and 80%.
4. The apparatus of claim 3 , wherein a size of the apertures is between 1 mm to 5 mm.
5. The apparatus of claim 4 , wherein the size of the apertures is about 1.9 mm.
6. The apparatus of claim 1 , wherein a pore opening of the pore is between 0.002 mm and 0.2 mm.
7. The apparatus of claim 6 , wherein the pore opening is 0.0345 mm.
8. The apparatus of claim 1 , wherein a thickness of the perforated steel plate is between 10 gauge and 18 gauge.
9. The apparatus of claim 8 , wherein the thickness of the perforated steel plate is about 16 gauge.
10. The apparatus of claim 1 , wherein a wire thickness of the wire mesh screen is between 0.14 mm to 0.1 mm.
11. The apparatus of claim 1 , wherein a wire thickness of the wire mesh screen is 0.28 mm.
12. The apparatus of claim 1 , wherein the desired separation distance provides a turbulence zone between the perforated steel plate and the wire mesh screen, whereby a turbulent exhaust gas flow in the turbulence zone orients a particulate fiber entrained in an exhaust gas flow in a non-perpendicular contact with the wire mesh screen.
13. A system for reducing particulate blockage of a catalyst bed in a coal fired refractory of a steam methane reformer, the coal fired refractory producing an exhaust gas flow in which a quantity of a refractory particulate (RP) contaminant and a stringed refractory fiber (RF) contaminant are carried in the exhaust gas flow, the exhaust gas flow carried within an exhaust shaft of the coal fired refractory having an outlet opening to the catalyst bed, comprising:
a dual screen element having a first stage, positioned in an upstream direction in the exhaust gas flow, and a second stage positioned in a downstream direction from the first stage, the dual screen element disposed at an offset angle from a longitudinal axis of the exhaust shaft, the dual screen element positioned upstream in the exhaust gas flow from the catalyst bed;
the first stage formed as a perforated steel plate having a plurality of apertures defined through a thickness of the perforated steel plate, the plurality of apertures defined in a spaced apart relation throughout a surface of the first stage, the perforated steel plate having a first open area ratio (OAR) between the plurality of apertures and the surface of the perforated steel plate of at least 30%; and
the second stage formed as a wire mesh screen having a second OAR between a pore and a mesh surface area of the wire mesh screen of at least 30%.
14. The system of claim 13 , wherein an area of the plurality of apertures is at least equal to a cross sectional area bounded by the exhaust shaft.
15. The system of claim 14 , wherein the first stage and the second stage are spaced apart by a separation distance in which a turbulence zone in the exhaust gas flow downstream from the first stage prevents the stringed RF from flowing in a perpendicular orientation relative to the second stage.
16. The system of claim 13 , further comprising:
a first blast of a plurality of air cannon oriented at a front surface of the dual screen element is directed at a high pressure and a low volume to clear accumulation of the RP and the RF from the dual screen element.
17. The system of claim 16 , further comprising:
a second blast of the plurality of air cannon oriented on a back surface of the dual screen element is regulated as a low pressure and a high-volume blast.
18. The system of claim 17 , wherein at least one of the first blast and the second blast convert the RF captured by the dual screen element to a particulate for entrainment with the exhaust gas flow through the catalyst bed.
19. The system of claim 13 , wherein the dual screen element is positioned in a vertical exhaust shaft upstream of the exhaust gas flow from a turn to a horizontal exhaust shaft.
20. The system of claim 13 , wherein the dual screen element is positioned in a horizontal exhaust shaft downstream from a turn from a vertical exhaust shaft.
21. A system for reducing particulate blockage of a catalyst bed in a coal fired refractory, the coal fired refractory producing an exhaust gas flow in which a quantity of a refractory particulate contaminant are carried in the exhaust gas flow, the exhaust gas flow carried within an exhaust shaft having an outlet opening to the catalyst bed, comprising:
a dual screen element having a first stage, positioned in an upstream direction in the exhaust gas flow, and a second stage positioned in a downstream direction from the first stage, the dual screen element disposed at an offset angle from a longitudinal axis of the exhaust shaft, the dual screen element positioned upstream in the exhaust gas flow from the catalyst bed;
the first stage formed as a perforated steel plate having a plurality of apertures defined through a thickness of the perforated steel plate, the plurality of apertures defined in a spaced apart relation throughout a surface of the first stage, when disposed at the offset angle, the perforated steel plate having an aperture opening area at least equal to a cross sectional area bounded by the exhaust shaft; and
the second stage formed as a wire mesh screen spaced apart from the first stage by a separation distance.
22. The system of claim 21 , wherein the separation distance provides a turbulence zone in the exhaust gas flow downstream from the first stage, wherein the turbulence zone prevents a stringed refractory fiber contaminant from flowing in a perpendicular orientation relative to the second stage.
23. The system of claim 21 , the dual screen element, further comprising:
a first open area ratio (OAR) between the plurality of apertures and the surface of the perforated steel plate of at least 30%; and
second OAR between a pore and a mesh surface area of the wire mesh screen of at least 30%.