AIR POLLUTION CONTROL ASSEMBLY AND METHOD

Abstract

An air pollution control assembly for treating flue gas streams containing acid gases. The assembly is comprised of an evaporative cooler assembly or a spray dryer gas distribution system. The assembly further has a reagent injection venturi assembly and a baghouse assembly. The baghouse assembly includes a filter cake management system which is automatically activated with respect to time and the pressure differential across the filter bags.

Description

BACKGROUND OF THE INVENTION

[0002] The present invention relates generally to air pollution control assemblies and particularly to assemblies and methods which control and treat gas streams to remove pollutants. Particularly, the invention relates to an air pollution control assembly for treating acid gas streams from incinerators and the like. More particularly, this invention relates to a synergistic combination of assemblies to effectively treat polluted gas streams.

[0003] In the past, various air pollution control apparatus and methods have been proposed and utilized in treating various flue gas streams. For example, Applicant's U.S. Pat. Nos. 3,876,402, 3,877,899, 4,105,421, 4,113,449 and 4,158,554 disclose apparatus and methods used to filter particulate laden gases. Fabric filtration structures and methods are generally disclosed directing particulate laden gas streams into baghouses. Structures and methods are also disclosed for cleaning filter bags of a baghouse as well as structures arranged to permit filtering elements to be replaced as a unit. These patents provide a background showing air pollution control equipment designs and methods.

[0004] Air pollution and environmental quality concerns continue to increase controls on industrial emissions via various laws, statutes, and mandates by regulatory agencies. The separation of undesirable particulate matter from effluent streams by fabric filtration is a method of controlling air pollution. Fabric filtration is performed using dust collection apparatus or baghouses which operate, except for scale, on the principle of vacuum cleaners. A baghouse is typically a sheet metal housing divided into two chambers, or plenums, by one or more tube sheets. Disposed within openings communicating with the plenums are fabric filters. A particle-laden gas stream, induced by a fan, for example, enters one chamber (dirty-air plenum) wherein dust accumulates on the fabric filter as the gas passes through the fabric into the other chamber (clean-air plenum) and out the exhaust. Although baghouses are typically designed in accordance with these principles, there are operational and structural differences between them. The present invention relates to a baghouse wherein the dirty and clean air plenums are separated by a tube sheet having a plurality of vertically suspended filter bags in which cylindrical wire cages are inserted for skeletal support. The gas is filtered as it moves from the outside of the bags to the inside. As a result, baghouses constructed in this manner are normally referred to as outside bag collectors.

[0005] It has been found desirable and necessary to precondition and treat gas streams prior to filtration. For example, flue gas streams with acid gases may damage and reduce the effectiveness of equipment and the acid gases are preferably removed or treated in the gas stream prior to and during filtration. By law, current codes require high efficiency removal of acid gases. One goal of the present invention is to comply with environmental laws to remove acid gases, such as HCl and SO2, from flue gas streams prior to and during filtration.

[0006] A filter or dust cake is the concentrated solid or semisolid material separated from the gas stream and which remains on the filter surface after filtration. A common method to remove dust cake from the bags is pneumatically flexing the bag with a quick, jet blast of air known as pulse jet bag cleaning. The method particularly relates to this invention and is accomplished by delivering a burst of compressed air into a venturi throat located in the clean-air plenum which directs the burst of air into the mouth of the bag, causing the bag to flex outwardly and dislodge the dust cake. In operation, the bags are cleaned in rows on a pre-selected cleaning cycle. The dislodged cake falls into the hopper and is removed from the baghouse by a screw conveyor.

[0007] The control of the filter cake thickness essentially controls the effectiveness of active reagent. Another object of the invention is to provide a baghouse cleaning method and to control the filter cake accumulated on the bag surfaces. The filter cake management system of the invention controls the filter cake on the bag surfaces to deal with any acid gases remaining in the flue gas stream.

SUMMARY OF THE INVENTION

[0008] The present invention provides an air pollution control assembly and method which relates to the treatment and removal of pollutants from gas streams. Specifically, the invention relates to an air pollution control assembly to treat flue gas streams having acid gases and other pollutants. The assembly comprises an evaporative cooler and/or spray dryer gas distribution system used to treat a gaseous stream to improve the removal of matter in air pollution control equipment. The assembly further provides a reagent injection venturi to treat a gaseous stream having an acidic gas content. The assembly and method also comprises a filter cake management system which enhances the removal of reactive and absorbable pollutants.

[0009] The object of this invention is to effectively and efficiently remove pollutants from gas streams, and particularly flue gas streams having acid gases. The evaporative cooler and spray dryer gas stream distribution system, the reagent injection venturi assembly, and filter cake management system may be individually utilized or may be used in combination with each other depending upon the nature of the flue gas streams to be treated.

[0010] These and other benefits of this invention will become clear from the following description by reference to the drawings.

DESCRIPTION OF THE DRAWINGS

[0011] FIG. 1 is a lateral plan view of the evaporative cooler assembly of the air pollution control equipment of the present invention; FIG. 2 is a lateral view of the assembly of FIG. 1 taken along line 2-2;

[0012] FIG. 3 is a sectional view of the nozzle assembly of the evaporative cooler assembly of FIG. 1;

[0013] FIG. 4 is a sectional view of the assembly of FIG. 1 taken along line 4-4;

[0014] FIG. 5 is a lateral plan view of the injection venturi assembly of the air pollution control equipment of the present invention;

[0015] FIG. 6 is a top plan view of the assembly of FIG. 5;

[0016] FIG. 7 is a front plan view of the baghouse assembly of the invention;

[0017] FIG. 8 is a lateral plan view of the baghouse assembly of FIG. 7;

[0018] FIG. 9 is a sectional view of the baghouse assembly of FIG. 8 and taken along line 9-9;

[0019] FIG. 10 is a sectional view of the baghouse assembly of FIG. 9 and taken along line 10-10;

[0020] FIG. 11 is a top plan view of the tube sheet used in the baghouse assembly of FIG. 7; and

[0021] FIG. 12 is lateral plan view of the ash removal system of the air pollution control equipment of the present invention.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0022] The present invention relates to air pollution control assemblies and methods and particularly to various air pollution control systems to treat gas streams to effectively and efficiently remove pollutants. The air pollution control assemblies are particularly adapted to remove acid gases from flue streams, such as those created in incinerators and the like. The assemblies of the invention involve several systems which are discussed below and these systems include an evaporative cooler and/or spray dryer gas distribution system, a reagent injection venturi assembly, and a filter cake management system.

[0023] Referring to FIGS. 1-4, the evaporative cooler gas distribution system is there shown. As shown in FIG. 1, the evaporative cooler gas distribution system 10 is comprised of an inlet plenum 11, an inlet orifice 12, water injectors 17 and air injectors 18, a diverging inlet section 13, a straight section 14 and a hopper section 15. The latter elements comprise the vessel 20.

[0024] In an evaporative cooler as shown in FIG. 1, water and air are injected by fluid distribution system 16 which is comprised of a plurality of spray lances having the water injectors 17 and air injectors 18 therein, to cool the gas stream to make it compatible with downstream air pollution control equipment, such as the reagent injection venturi 30 and baghouse filtration assembly 40. As shown, the fluid distribution system 16 is placed in the inlet section 13 of vessel 20. The spray lances include the piping and nozzles connected to injectors 17 and 18 as shown in FIG. 3. The spray lances protrude into vessel 20 and are constructed and arranged to uniformly disburse fluid into the gas stream. Evaporative coolers and spray dryers are similar devices and the device features may be combined in the fluid distribution system 16 or alternatively, the spray dryer may be located downstream from system 16. In a spray dryer (not shown), a slurry of a reagent, water and air are injected into the vessel 20 to cool the gas stream, and to cause a reaction between the reagent and acid gases in the flue gas stream. Hydrated lime, sodium bicarbonate or other reactive chemicals, for example, may be used as reagents to treat multiple pollutants, including heavy metals, for example. The reagents may be injected through the water injectors or may be separately introduced in the center of the vessel 20.

[0025] In both evaporative coolers and spray dryers, it is imperative that all of the liquid be completely evaporated in the vessel 20 to prevent fouling of the air pollution control equipment, and it is also necessary that the flue gas is uniformly treated to preclude stratified temperature regions or unreacted acid gas. Therefore, the flue gases are evenly distributed across the vessel, with uniform flow that is parallel to the vessel walls. The distribution is done as quickly as possible, and generally must be done while the flue gas makes a 90° turn while entering the vessel. Furthermore, the quality of the gas distribution must be maintained while the gas flow varies by as much as 30%. Because the gas temperature may be 2000° F. or more, it is not practical to use internal gas distribution means, such as turning vanes.

[0026] The present invention relates to a system for distributing water having a distribution system 16 at the inlet to the evaporative cooling/spray drying vessel 20 that meets the above described requirements. The flue gas enters a plenum where the gas velocity is reduced. An orifice 12 forms an opening into vessel 20 and is located at 90 degrees to the inlet gas flow. This orifice 12 creates a sufficient pressure drop between inlet plenum 11 and vessel 20 to throttle the gas flow and cause the flow pattern to be dictated by pressure relief rather than inertia. Therefore, the gas flows from plenum 11 through orifice 12 with uniform distribution over the cross sectional area.

[0027] The cooling/spray drying vessel 20 has walls defining a diverging inlet section 13, that flare outward at a nominal included angle of 15 degrees, which is generally equal to the natural expansion of a gas. Water is then injected, preferably uniformly, into the gas by means of distribution system 16 comprised of at least one injector located in the side wall of diverging inlet section 13. The vessel 20 may also have at least a reagent slurry injector assembly located below the water injector, for applying reagent while cooling the gas stream. The system preferably has water injectors 17 and air injectors 18. The air injectors are used to atomize the water particles allowing them to combine with the gas particles in the stream to effectively cooling the gas particles. Preferably, the water/air and or reagent injectors are centrally positioned in the vessel to cocurrently introduce the fluids with the flue gas flow. For example, a pattern of a plurality, i.e., 3 or 4 injectors may be used. The diverging inlet section 13 opens into a straight section 14 further allowing the gas to expand and cool. The gas then enters a converging hopper section 15 where heavier particles fall into the bottom of hopper 15 and lighter particles continue through the air filtration system by exiting the vessel 20 through flue gas outlet 19.

[0028] Referring to FIGS. 5 and 6, the reagent injection venturi assembly of the present invention is there shown. To achieve a high acid gas removal efficiency, it is necessary that the reagent that is injected be uniformly distributed across the gas stream, so that contact is made with all of the acid gases and pollutants generated in the incinerator. This distribution must be effective, regardless of normal fluctuations in the gas volume (30% typically). Furthermore, since reagents and reactants are often self adherent and subject to build-up, in order to operate reliably, the gas distribution device must cause smooth flow lines and require that a minimum amount of equipment be located in the gas stream.

[0029] The present invention relates to a device that meets these requirements. As shown in FIGS. 5 and 6, the ductwork at the point of injection is comprised of a converging acceleration section 32, a short straight high velocity section 33, and a diverging deceleration section 34, effectively creating a venturi shape with a “neck” or straight section 33 in the center of the assembly 30. The reagent is piped into the center of the injection venturi by reagent injector 36, at the converging section, where it may be either blown or sucked into the flue gas stream.

[0030] As shown in the drawings, the injection is cocurrent to the flue gas flow to reduce fall out in the duct. The rapid acceleration in converging section 32, and high speed flow in high velocity section 33 causes turbulence that mixes the reagent with the gas stream. The narrow angle of expansion in diverging acceleration section 34 allows the reagent to expand with the gas stream, keeping it well distributed.

[0031] Referring to FIGS. 7-12, the filter cake management system of the present invention is implemented in a baghouse filtration assembly 40. Generally, the flue gas enters the baghouse assembly 40 through horizontal hopper inlet 41, preferably located in the side wall of hopper 42. Inside the assembly 40, heavier particles fall into hopper 42 for removal at outlet 49, while lighter particles travel through dirty gas chamber 51 and are filtered by filter bags 50. The bags 50, preferably are disposed around the exterior of filter tube cages 47 which are preferably hanging down from a filter tube sheet 45 within housing section 44. The tube sheet 45 is supported by tube sheet support members 46 attached to housing section 44. Once the gas is filtered by filter bags 50, the gas travels through clean gas plenum 52 and out the clean gas outlet 48.

[0032] The accumulation of particulate on the surface of a filter bag in a baghouse filtration assembly 40 as shown in FIGS. 7, 8, and 12 is referred to as the “filter cake.”This cake has long been recognized as being an important aid in effective filtration of particulate. In the case of a dry scrubber system where a reagent is injected into the gas steam to react with acid gasses, it performs an additional function. Because the gas flow is relatively slow as it passes through the filter cake, and contact is intimate with the reagent, it is a critical component of the acid gas scrubbing program.

[0033] In order to maximize the filter cake's effectiveness, it is important to accomplish several things simultaneously: a reasonably thick cake should be retained (but not enough to unduly impede gas flow); the reacted material in the filter cake needs to be removed periodically; the unreacted material needs to be retained and replenished; the proper density of the filter cake needs to be continuously maintained; and all of these conditions must occur equally on all bags and throughout the length of every bag.

[0034] The present invention relates to a system comprised of several baghouse features that collectively accomplish the above described requirements. The system of this invention consists of a gas distribution device (ladder vane baffle) 43 that is located in the hopper 42 of baghouse 40 as the gas enters from horizontal hopper inlet 41. This device in effect functions as a series of turning vanes to direct the gas and reagent flow inlet 41 and distribute it evenly throughout dirty gas chamber 51. It is arranged to minimize the amount of reagent that is knocked out of the gas stream, and also has no flat horizontal surfaces for material build-up. The baghouse sizing, bag spacing, and bag length to diameter ratio are all established so that the upward gas velocity between the bags 50 is such that larger particles can fall against the gas flow and reach the hopper 42 for removal, while smaller, less dense particles are retained and deposited back on bags 50. This is significant because as particles reside in the baghouse and react with the acid gases, they tend to agglomerate and grow. These aged particles have reacted and are of no further benefit, so their removal is desirable. On the other hand, the smaller particles tend to be new, fresh reagent, and it is beneficial for them to be retained and remain as a part of the filter cake for continued reaction.

[0035] The bags 50 are cleaned automatically to prevent the baghouse 40 from becoming clogged. The cleaning methodology is critical to maintaining the effectiveness of the acid gas reaction in the filter cake, If bags 50 are cleaned too often or too effectively, there will be a period when there is an insufficient amount of reagent in the filter cake for maximum effectiveness. If bags 50 are not cleaned often enough, the reagent in the inner part of the filter cake reacts with the gas and becomes ineffective, while new reagent that is added to the outside of the filter cake will often shed or flake off before it has a chance to react. These problems are solved by initiating bag cleaning automatically by two different parameters. A differential pressure sensor (not shown) monitors the differential pressure across the system and will initiate cleaning when bags 50 have accumulated a sufficient amount of material that it impedes flow, which also is related to the amount of pollutants that the system has handled. If the pressure differential has not initiated bag cleaning in a preset period, a timer will instead initiate the cleaning. This prevents the system from going too long without rejuvenating the filter cake. Also, only a fraction of bags 50 are cleaned with each initiation so the entire filter cake is never removed in a single cleaning episode. For example, selected rows or bags are cleaned at a time by a pulse jet to control filter cake build up thickness. The timer, pressure differential, and number of bags cleaned are all determined individually on each project based on experience and the specific operating parameters.

[0036] The invention also utilizes control ladder logistics that provides an electrical description relating to the process used in the monitoring and operation of the bag cleaning system of this invention. A computerized system may be provided to control the operation of water pumps, fans, valves, temperature controls, timers, alarms, etc. which are used in the assembly of this invention.

[0037] When the differential pressure sensor or the timer indicate that the bag filters need to be cleaned, the normal baghouse filtration operation may continue to run or may be interrupted allowing the pressure differential to fall to make the removal of particulate from the filters easier. Air is pulsed into a predetermined percentage of the bag filters within the baghouse to blow the loosened particulate from the filters. Preferably, a compressed air injector or blowpipe 53 is aligned with each row of filter bags or another preselected number of bags. The selected bags are pulsed to jar the loosened material reducing the thickness of the filter cake on the selected bags.

[0038] The removed particulate falls from the filters into the hopper. The hopper is then cleaned by a screw conveyor ash removal system connected at the hopper outlet. As the particulate is being removed, the hopper is preferably vibrated to ensure that the maximum amount of particulate is removed.

[0039] Fresh reagent is applied to the filter bags by the flue gas having reagents previously injected into the flue gas stream. In summary, the cleaning process includes pulsing the individual rows of bags to dislodge filter cake, settling of the dislodged material into the hopper for removal, and reestablishment of a reactive filter cake.

[0040] As many changes are possible to the embodiments of this invention utilizing the teachings thereof, the description above, and the accompanying drawings should be interpreted in the illustrative and not the limited sense.

Claims

1. An air pollution control assembly for treating a flue gas stream comprising: a) an evaporative cooler assembly for injecting fluid across said flue gas stream, said cooler assembly including means to direct said flue gas stream; b) a reagent injection venturi assembly having converging and diverging sections and wherein a reagent is injected cocurrent with the flue gas in said converging section; and c) a baghouse assembly having an inlet and a gas distribution device positioned at said baghouse inlet, said baghouse further having a plurality of filter bags and a filter cake management system.

2. The air pollution control assembly of claim 1, wherein said evaporative cooler includes an injector assembly for spraying a reagent into said flue gas stream to react with acid gases in said flue gas stream.

3. The air pollution control assembly of claim 2, wherein said cooler assembly comprises a vessel having a wall and an inlet and wherein said inlet is constructed and arranged to turn the flow of said flue gas approximately 90 degrees whereby said gas is directed generally parallel to said vessel wall and evenly distributed across said vessel.

4. The air pollution control assembly of claim 3, wherein said vessel inlet includes a gas distribution system comprising a plenum having an orifice disposed approximately 90 degrees with respect to the plenum inlet flow.

5. The air pollution control assembly of claim 3, wherein said evaporative cooler includes a water and air injector and a reagent injector.

6. The air pollution control assembly of claim 3, wherein said vessel wall slopes outwardly from said inlet at a cross-sectional angle of approximately 15 degrees.

7. The air pollution control assembly of claim 1, wherein said reagent injection venturi assembly includes a reagent pipe having an end positioned generally centrally said flue gas stream at said converging section whereby reagent is injected cocurrent with said flue gas stream.

8. The air pollution control assembly of claim 1, wherein said gas distribution device of said baghouse assembly is a ladder vane baffle device.

9. The air pollution control assembly of claim 1, wherein said filter bags of said baghouse assembly have a surface for the accumulation of filter cake and wherein said filter cake management system includes means to measure pressure differential in said baghouse assembly.

10. The air pollution control assembly of claim 9, wherein said filter cake management system includes a timer to initiate bag cleaning.

11. An air pollution control assembly for treating a flue gas stream comprising: a) a reagent injection venturi assembly having converging and diverging sections and wherein a fluid injector is positioned at said converging section, said fluid injector including a reagent pipe having an end positioned generally centrally of said flue gas stream at said converging section whereby reagent is injected cocurrent with said flue gas stream; and b) a baghouse assembly having an inlet and a gas distribution device positioned at said baghouse inlet, said baghouse further having a plurality of filter bags and a filter cake management system and wherein each said filter bag has a surface for the accumulation of filter cake and wherein said filter cake management system includes means to measure pressure differential across said filter bags in said baghouse assembly.

12. The air pollution control assembly of claim 11, wherein said fluid is a reagent for reacting to acid gases in said gas stream.

13. The air pollution control assembly of claim 11, wherein said gas distribution device of said baghouse assembly is a ladder vane baffle device.

14. The air pollution control assembly of claim 13, wherein said filter cake management system includes a timer and a pressure differential measuring means to initiate bag cleaning.

15. An air pollution control assembly comprising: a) an evaporative cooler apparatus having at least one wall forming a tube-like structure, a gas flow inlet structure, said flow inlet structure having a gas stream distribution system comprised of a plenum having at least one wall flaring out from said orifice arranged at approximately a 90 degree angle from said orifice and constructed and arranged to taper outwardly at a predetermined nominal angle, said system further comprising a fluid distribution means constructed and arranged to distribute a uniform amount of fluid cocurrent with said gas; b) a reagent injection venturi comprised of at least one wall and having a central axis therethrough, said venturi comprised of a gas flow inlet wherein said at least one wall tapers inward toward said central axis to form a converging section, said at least one wall tapering to become aligned parallel with said central axis forming a straight section and said at least one wall then tapering outward away from said central axis to form a diverging section, said venturi having a reagent injection means positioned in said converging section to introduce a reagent cocurrent to said gas stream; c) a filter bag-house having a filter cake management system, said bag-house comprised of a gas flow inlet having at least one wall and having a gas distribution device, a clean air plenum and a dirty air plenum separated by a plurality of filter bags having a predetermined size, spacing, and length-to-diameter ratio, a bag cleaning mechanism having a means to monitor a pressure differential between the pressure inside the filter bags and outside the filter bags, said means to monitor pressure differential triggers the initiation of a cleaning sequence on a predetermined percentage of filter bags when said means to monitor pressure differential indicates that flow is being impeded, said bag cleaning mechanism further comprising a timer having a predetermined time period that initiates cleaning if said means to monitor pressure differential has not initiated the cleaning sequence within said predetermined time period.

16. An assembly for treating and removing pollutants from a gas stream comprising: a) a plurality of gas stream flow control assemblies; b) a plurality of fluid nozzle assemblies constructed and arranged to treat said gas stream; c) a plurality of gas stream filtering assemblies for producing filter cake surfaces; and d) means to control said filter cake surfaces.

17. The assembly of claim 16, wherein said gas stream flow control assemblies include at least one ladder vane baffle, a plenum assembly and a venturi device.

18. The assembly of claim 16, wherein said fluid nozzle assemblies include a water source, a compressed air source and a reagent slurry.

19. The assembly of claim 16, wherein said gas stream filtering assemblies include fabric filter bags having flexible surfaces and wherein said filter bags are disposed in a series of rows.

20. The assembly of claim 19, wherein said means to control said filter cake surfaces include air pressure jets cooperating with each said filter bag, a timer and a pressure differential sensing device.