阅读说明：本技术 使用具有堆叠气流间隙的***组件的系统和方法 (Systems and methods using insert assemblies with stacked airflow gaps ) 是由 W·R·佩克拉 D·A·费舍尔 于 2015-03-10 设计创作，主要内容包括：本发明公开具有堆叠气流间隙以从行进穿过屏障的固体/气体混合物添加及/或移除气体的插入组件。实例系统可包含屏障及所述屏障中的插入组件,所述屏障限定所述插入组件与所述屏障之间的环形区,其中所述插入组件包含配置成从所述环形区中流动的固体/气体混合物添加及/或移除气体的堆叠流体间隙。(Insert assemblies having stacked gas flow gaps to add and/or remove gas from a solid/gas mixture traveling through a barrier are disclosed. An example system may include a barrier defining an annular region between the insert and the barrier and an insert component in the barrier, wherein the insert component includes a stacked fluid gap configured to add and/or remove gas from a solid/gas mixture flowing in the annular region.)

1. A method for purging a solid/gas mixture, comprising:

adding the solid/gas mixture to a barrier having an insert component therein, wherein the insert component comprises a stacked fluidic gap;

injecting a flushing gas through the insert assembly and into the solid/gas mixture as the solid/gas mixture moves downward through the barrier; and

removing gas from the solid/gas mixture through the insert assembly as the solid/gas mixture moves downward through the barrier.

2. The method of claim 1, wherein the insert assembly is configured such that the solid/gas mixture flowing in the barrier has about a constant velocity profile thereacross.

3. The method of claim 1 or 2, wherein the insert assembly comprises a series of stacked inverted cones, and wherein the injecting the purge gas comprises injecting the purge gas into a region below an uppermost of the stacked inverted cones.

4. The method of claim 2 or 3, wherein the insert assembly comprises an inverted cone and a member below the inverted cone, and wherein the injecting the purge gas comprises injecting the purge gas into a region below the inverted cone.

5. The method of claim 4, wherein the removing the gas comprises removing gas from an uppermost section of the member, wherein a tapered portion of the uppermost section extends into the inverted cone.

6. The method of claim 4 or 5, wherein the removing the gas includes flowing the gas through the stacked fluid gaps formed between sections of the component.

7. The method of any one of claims 1-6, wherein the removing the gas comprises flowing the gas through a skirt extending inwardly from the insert assembly.

8. The method of any of claims 1-7, wherein the stacking gaps have a vertical spacing of about 12 inches or less, and wherein the stacking gaps each have a width of about r/2 to about r/5, where r is a radius of the insert assembly.

Technical Field

The present invention generally relates to adding and/or removing gas from a solid/gas mixture flowing through a barrier. In particular, the present invention relates to the use of insert assemblies having stacked gas flow gaps in a barrier to add and/or remove gas from a solid/gas mixture traveling through a vessel.

Background

Typically, polyolefin polymerization processes utilize a flush bin after the reaction vessel to remove unwanted volatiles from the polymer resin. A purge bin is a container in which a resin mixture enters an upper portion of the container and undergoes an purging gas through a port or opening at the bottom of the container and possibly other areas along the side of the container to remove volatiles by purging.

However, simply piping the purge gas into the resin without regard to the solid fluid distribution, the distribution of the purge gas through the resin, the resin flow pattern, and any potential thermal effects of the purge gas may result in damage to the resin and may produce undesirable or commercially non-viable polymer products. In addition, the time that the resin is exposed to the purging gas may also affect the degree of volatile removal from the resin.

The interface between the resin and the flush bin and any associated protrusions (such as pipes, sleeves, supports, etc. that may protrude into the resin flow path) may also contribute to the flow rate of the resin through the flush bin. Since the resin can be flushed from volatiles at a rate depending on the contact time between the resin and the flushing gas, any non-uniform flow pattern of the resin (i.e., slower or faster resin flow) can affect the amount of volatiles flushed. Thus, the amount of volatiles removed differs from one section of the washout bin to another depending on the flow pattern of the resin.

Insert assemblies through which gas can be added and/or removed from the flow path of the resin are typically included in the purge bin to address some of these issues with respect to mass flow in the purge bin and gas distribution within the solids bed. One example of an insert assembly includes an inverted cone having one or more cylindrical component sections below it with the purpose of achieving a nearly constant velocity profile of the resin traveling downward in the wash tank. Other types of insertion assemblies may also be included in the flush cartridge. However, by including the insertion assembly in the flush cartridge, the cartridge diameter may undesirably increase, thus increasing cartridge cost. This is because the diameter of the flush bin is a function of the area of the insert assembly. This relationship between the silo diameter and the insertion area arises because the maximum skin velocity must not be exceeded without unacceptably high amounts of resin entrainment occurring with the removal of gas from the solid bed. Resin entrained in the extraction gas may be undesirable for downstream equipment and may lead to pipe fouling. Furthermore, local fluidization of solids when introducing gas into a bed of solids is also undesirable as it can lead to gas maldistribution, disruption of the solids flow, and separation.

Disclosure of Invention

An example system disclosed herein includes a barrier defining an annular region between the insert component and the barrier, and an insert component in the barrier, wherein the insert component includes a stacked fluid gap configured to add and/or remove gas from a solid/gas mixture flowing in the annular region.

Example methods disclosed herein are for purging a solid/gas mixture. The method may include adding a solid/gas mixture to the barrier having an insert element therein, wherein the insert element includes a stacked fluidic gap. The method may further include injecting a flushing gas through the insert component and into the solid/gas mixture as the solid/gas mixture moves downward through the barrier. The method further may include removing gas from the solid/gas mixture through the insert assembly as the solid/gas mixture moves downward through the barrier.

The foregoing has outlined rather broadly the features and technical advantages of the present invention in order that the detailed description of the invention that follows may be better understood. Additional features and advantages of the invention will be described hereinafter which form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and specific embodiment disclosed may be readily utilized as a basis for modifying or designing other embodiments for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent embodiments do not depart from the spirit and scope of the invention as set forth in the appended claims.

The invention comprises the following steps:

1. a system, comprising:

a barrier; and

an insert element in the barrier defining an annular region between the insert element and the barrier, wherein the insert element comprises a stacked fluidic gap configured to add and/or remove gas from a solid/gas mixture flowing in the annular region.

2. The system of item 1, wherein the insert assembly is configured to cause the solid/gas mixture flowing in the annular region to have about a constant velocity profile thereacross.

3. The system of clauses 1 or 2, wherein the insert assembly comprises a series of stacked inverted cones.

4. The system of any preceding claim, wherein the insert assembly comprises an inverted cone and a component below the inverted cone.

5. The system of item 4, wherein the component comprises: having an uppermost member section extending into the inverted cone; an intermediate component section extending into a lower portion of the uppermost component section; and a lowermost component section having a tapered portion extending into a lower portion of the intermediate component section.

6. The system of clause 5, wherein the intermediate member segment tapers from bottom to top.

7. The system of clauses 5 or 6, wherein the chambers in the uppermost intermediate section are not in fluid communication with the chambers in the inverted cone, and wherein the cavities in the intermediate member section are in fluid communication with the chambers in the uppermost intermediate section.

8. The system of any of clauses 4 to 7, further comprising a gas inlet for delivering a purge gas to the region below the inverted cone; and a gas outlet for conveying gas from a region in the uppermost component section.

9. The system of any preceding claim, further comprising a skirt extending inwardly from the insert component for each of the stacking gaps.

10. The system of any of claims 1-8, further comprising a skirt extending outwardly from the insert assembly for each of the stacking gaps.

11. The system of any preceding claim, wherein the stack gap has a vertical spacing of about 12 inches or less from an adjacent one of the stack gaps.

12. The system of any preceding claim, wherein the stacking gaps each have a width of about r/2 to about r/5, where r is a radius of the insert assembly.

13. A method for purging a solid/gas mixture, comprising:

adding the solid/gas mixture to a barrier having an insert component therein, wherein the insert component comprises a stacked fluidic gap;

injecting a flushing gas through the insert assembly and into the solid/gas mixture as the solid/gas mixture moves downward through the barrier; and

removing gas from the solid/gas mixture through the insert assembly as the solid/gas mixture moves downward through the barrier.

14. The method of item 13, wherein the insert assembly is configured to cause the solid/gas mixture flowing in the barrier to have about a constant velocity profile thereacross.

15. The method of clauses 13 or 14, wherein the insert assembly comprises a series of stacked inverted cones, and wherein the injecting the purge gas comprises injecting the purge gas into a region below an uppermost of the stacked inverted cones.

16. The method of clause 14 or 15, wherein the insert assembly comprises an inverted cone and a member underlying the inverted cone, and wherein the injecting the purge gas comprises injecting the purge gas into a region underlying the inverted cone.

17. The method of clause 16, wherein the removing the gas comprises removing gas from an uppermost section of the member, wherein a tapered portion of the uppermost section extends into the inverted cone.

18. The method of item 16 or 17, wherein the removing the gas comprises flowing the gas through the stacked fluid gaps formed between sections of the component.

19. The method of any of items 13 to 18, wherein the removing the gas comprises flowing the gas through a skirt extending inwardly from the insert assembly.

20. The method of any of clauses 13-19, wherein the stacking gaps have a vertical spacing of about 12 inches or less, and wherein the stacking gaps each have a width of about r/2 to about r/5, wherein r is a radius of the insert assembly.

Drawings

For a detailed description of the preferred embodiments of the invention, reference will now be made to the accompanying drawings in which:

fig. 1 is an exemplary cross-sectional view of a system for adding and/or removing gas from a solid/gas mixture.

Fig. 2 is an exemplary cross-sectional view of a system for adding and/or removing gas from a solid/gas mixture.

Fig. 3 is an exemplary cross-sectional view of a system for adding and/or removing gas from a solid/gas mixture.

Fig. 4 is an exemplary cross-sectional view of an insert assembly for adding and/or removing gas from a solid/gas mixture in a flush bin.

Fig. 5 is an exemplary cross-sectional view illustrating indentations in an insert assembly for adding and/or removing gas from a solid/gas mixture.

Detailed Description

While the present compounds, components, ingredients, devices, apparatus, configurations, schematics, systems and/or methods have been disclosed and described previously, it is to be understood that this invention is not limited to specific compounds, components, ingredients, devices, apparatus, configurations, schematics systems, methods or the like, unless otherwise specified, and thus can be varied. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting.

It must also be noted that, as used in the specification and the appended claims, the singular forms "a," "an," and "the" include plural referents unless the context clearly dictates otherwise.

In general, embodiments disclosed herein relate to methods and systems for adding and/or removing gas from a flush bin. For example, embodiments disclosed herein relate to systems and methods for removing volatiles from resin in a "plug flow" manner as the resin flows through a mass flow wash bin.

Other general embodiments include methods for purging gas from a solid/gas mixture, wherein the solid/gas mixture flows through a purge bin, contacting an insert assembly comprising an inverted cone (having a component below the cone). In some embodiments, the solid/gas mixture flowing through the flush bin may have a nearly constant velocity profile. Embodiments herein further include stacked fluid gaps in the insert assembly for adding and/or removing gas from the solid/gas mixture. For example, a purge gas may be added to the solid/gas mixture through the stacked fluid gaps.

As used herein, the term "flush" refers to a process that removes unwanted dissolved and undissolved gases (including hydrocarbons and/or volatiles) from a solid crystalline polymer having gas-filled interstitials. In addition to the interstitial gases, hydrocarbons may be dissolved in the resin. The purging operation generally includes generating sufficient power to diffuse the adsorbed hydrocarbons from the resin. The interstitial hydrocarbons are rapidly displaced by the purge gas, but the dissolved hydrocarbons slowly evolve (the macromolecules diffuse out more slowly) through a relative diffusion rate that depends on the Molecular Weight (MW) of the hydrocarbons.

As used herein, the term "volatile" refers to a component or compound having a low relative boiling point as compared to its surrounding components or compounds. Illustrative volatiles include, but are not limited to, nitrogen, water, ammonia, methane, carbon dioxide, and all compounds of oxygen, carbon, and hydrogen.

As used herein, the term "solid" refers to any solid material, such as resins, granules, metal particles, and the like. For example, the solids included in the solid/gas mixture may be polymeric resin that has been treated to form a polymer that includes volatiles to be removed prior to storage or further treatment of the resin.

As used herein, the term "solid/gas mixture" refers to any substance including any solid, liquid, or gaseous substance (including any mixture thereof). For example, a solid/gas mixture may refer to a mixture of volatile gas, polymeric resin, and purge gas, or in some cases, it may refer to only polymeric resin and/or purge gas, and so forth.

As used herein, the term "resin" refers to an intermediate or final material in the polymerization process. The resin may be a solid or a mixture of a solid and one or more interstitial gases. For example, the resin may include any olefin monomer, including substituted and unsubstituted olefins having from two to 10 carbon atoms, such as ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, 1-decene, 1-dodecene, styrene, and derivatives and mixtures thereof, as well as other impurities such as volatiles, liquids, and the like. Both unreacted monomer (alkene) and unreacted alkane may be dissolved in the resin and both alkane and alkene may include a portion of the interstitial gas. Illustrative non-reactive alkanes include, but are not limited to, propane, butane, isobutane, pentane, isopentane, hexane, isomers thereof, and derivatives thereof.

As used herein, the term "mass flow" refers to a unique fluid condition in which the smooth surfaces and steep slopes of the vessel enable all of the solids in the vessel to be in motion as the solids are discharged from the vessel.

As used herein, the term "plug flow" refers to a subset of mass flow wherein substantially all of a certain material, solid, gas, liquid, or combination thereof in a vessel has about a uniform velocity profile at a given point. For example, in a vertically oriented flush bin, plug flow may be obtained when the solid/gas mixture in the flush bin travels vertically downward at a given level at substantially the same velocity. In another example, in a vertically oriented flush bin, plug flow may be obtained when one or more solids in a solids/gas mixture travel vertically downward at approximately the same velocity at a given level in the flush bin.

As used herein, the term "surface interface" refers to the contact area between a gaseous environment and the surface of a solid semi-solid material. For example, downstream from each gas injection point, there may be a region of the solid/gas mixture where the injected gas interacts with the surface of the solid/gas mixture.

As used herein, the term "constant velocity profile" refers to, for example, one or more solids in a medium such as a solid/gas mixture at a given level in a preferably vertically oriented flush bin traveling downward (vertically downward in one class of embodiments) in the flush bin at or about the same velocity as the form velocity. As used herein, the term "constant vertical velocity profile" refers to, for example, one or more solids in a medium such as a solid/gas mixture at a given level in a vertically oriented washhouse traveling vertically downward at the same or about the same velocity in the washhouse.

Referring now to fig. 1, a system 100 for adding and/or removing gas from a solid/gas mixture in a barrier is shown, which may be a silo, a casing, a pipe, etc., wherein the barrier may have any cross-sectional shape, such as circular, elliptical, polygonal, etc. For simplicity, and without limiting the invention in any way, the barrier has been depicted in fig. 1-3 as a flush bin 102, and the full description of the figures accompanying the barrier refers to the flush bin when referring to the barrier. However, the flush cartridge 102 is interchangeable with any type of barrier in the following description without affecting the scope and breadth of the present invention.

In the illustrated embodiment, the flush cartridge 102 includes an upper inlet 104 located at or near an upper portion of the flush cartridge 102. The solid/gas mixture may enter the flush bin 102 through the upper inlet 104. As previously described, the solid/gas mixture may, in some embodiments, include a resin that may contain unnecessary dissolved and undissolved gas. The solid/gas mixture may flow through the flush bin 102 in the direction indicated by arrow 106. As illustrated, the flush cartridge 102 may further include a lower discharge 108 located at or near a lower portion of the flush cartridge 102. In the illustrated embodiment, the lower portion of the flush cartridge 102 can include a tapered portion 103, which can be, for example, conical in shape. The solid/gas mixture may exit the flush bin 102 through a lower discharge 108. Although only the upper inlet 104 and the lower discharge 108 are illustrated on fig. 1, more than one inlet and outlet is possible, and several fluids may be used in the flush bin 102 as well as other ways of handling the fluids of the solid/gas mixture.

The purge bin 102 may include a gas inlet 110 through which purge gas may be added to the solid/gas mixture. As illustrated, the gas inlets 110 may be located in the upper and lower portions of the washout bin 102. One or more of the gas inlets 110 can introduce the flushing gas into the flush bin 102 through a skirt 111 positioned on an inner wall of the flush bin 102 at the gas inlet 110. The angle of the skirt 111 may be steep enough to allow the solid/gas mixture to slide over the outer surface of the skirt 111 surface and may contribute to the solid mass flow. The skirt 111 may completely surround the surface perimeter of the inner wall of the flush bin 102. In some embodiments, skirt 111 may be segmented, and these segmented skirts may be placed at different positions relative to the longitudinal axis of flush cartridge 102, or may be placed at the same position relative to the longitudinal axis of flush cartridge 102.

Each of the skirt 111 and/or flush bin 102 walls may comprise a friction reducing coating on at least the outer solid/gas mixture contacting surface. Illustrative friction reducing coatings include fluoropolymers such as Polytetrafluoroethylene (PTFE), fluorinated ethylene-propylene (FEP), PLASITE7122VTF, and the like. Some of the coatings are preferred to

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The skirt 111 may be formed by having a smaller inner diameter adjacent an upper portion of the flush bin 102 and a larger inner diameter adjacent a lower portion of the flush bin 102, defining a gap therebetween for transporting gas to or from the solid/gas mixture within the flush bin 102, as shown in fig. 1.

The purge bin 102 may also include an insert gas inlet 112 through which purge gas may be added to the solid/gas mixture by way of an insert assembly 114. The flush bin 102 may include a filter 116 through which gas may be removed from the flush bin 102. In some embodiments, a portion of the gas may flow out of filter 116, and in alternative embodiments, substantially all of the gas may flow out of filter 116. However, the gas may flow out of substantially any extraction point in the flush bin 102. For example, the flush cartridge 102 may include an insert gas outlet 118 for extracting gas from the flush cartridge 102 through the insert assembly 114.

The flush cartridge 102 may include an insert assembly 114. As illustrated, the insert assembly 114 may include an inverted taper 120 and a member 122 below the inverted taper 120. As illustrated, an annular space 124 can be formed between the flush cartridge 102 and the insert assembly 114. The gas/fluid mixture may flow downward through the flush bin in the annular space 124. The member 122 below the reverse taper 120 may be sized to pass the solid/gas mixture there along to have approximately a constant velocity profile there across. The angle of the inverted cone 120 may be steep enough to allow the solid/gas mixture to slide on the outside of the exterior surface of the inverted cone 120 and may contribute to the solid mass flow. The top of the inverted cone 120 may be pointed, curved, flat, or otherwise formed as desired for a particular application. In some embodiments, the insert assembly 114 may be used to maintain a close plug flow in the annular space 124. The reverse taper 120 and/or the member 122 may have any cross-sectional shape, such as circular, elliptical, polygonal, and the like. Further, the inverted cone 120 and/or member 122 may have a pointed end, a rounded end, a square end, and the like. In some embodiments, the reverse taper 120 may have a steep angle and a smooth surface such that mass flow is facilitated in the flush bin 102. The insert assembly 114 may facilitate solid mass flow around its exterior surface by having a smooth surface.

Member 122 may be comprised of any number of member segments, such as member segments 126, 128, 130, which may be included below reverse taper 120. The arrangement, design, and selection of selected ones of the component sections 126, 128, 130, including the reverse taper 120, if present, are each a decision depending on the desired overall effect of the insert assembly 114 and the number and distribution of air inlets and extraction points. One or more of the component sections 126, 128, 130 may be used for any insert assembly 114 depending on several factors including the length of the flush bin 102, the flow rate of the solid/gas mixture, the gas flow rate, and the like. These component sections 126, 128, 130 are referred to herein as an uppermost component section 126, an intermediate component section 128, and a lowermost component section 130. As illustrated, the reverse taper 120 may be a separate piece from the uppermost member section 126. The reverse taper 120 may also be part of the uppermost member section 126, e.g., may be an upper terminus of the uppermost member section 126. Additionally, the annular space 124 can be a portion of the flush cartridge 102, such as an extension, or it can be a separate portion.

The uppermost member section 126 may have a generally constant diameter, for example, the uppermost member section 126 may be generally cylindrical in shape. However, other suitable shapes having a substantially constant cross-sectional area may be suitable. In the illustrated embodiment, the uppermost component section 126 includes a tapered portion 127 at an upper end thereof. As illustrated, this tapered portion 127 may extend into a bottom portion of the inverted cone 120. The uppermost member section 126 may also be configured to add or remove gas from the surface interface of the solid/gas mixture. In the illustrated embodiment, uppermost component section 126 includes an insert gas outlet 118 for extracting gas.

Intermediate member segment 128 may be disposed at least partially between uppermost member segment 126 and lowermost member segment 130. Although not shown, additional member segments may also be disposed above or below the intermediate member segment 128 between the uppermost member segment 126 and the lowermost member segment 130. In the illustrated embodiment, the intermediate member segment 128 extends into the bottom of the uppermost member segment 126. As illustrated, the intermediate member segment 128 may taper from bottom to top. The intermediate member section 128 may also be conical in shape with a top that is curved, pointed, flattened, or otherwise formed. However, other shapes that taper from bottom to top may also be suitable. Additionally, only a portion of the intermediate member section 128 may be conically shaped, wherein a portion of the intermediate member section 128 may have a generally constant cross-sectional area. The intermediate member section 128 may also be configured to add or remove gas from the surface interface of the solid/gas mixture. In the illustrated embodiment, the intermediate member section 128 communicates with the uppermost member section 126 for gas extraction.

The lowest component section 130 may be disposed at least partially below the middle component section 128. The lowest member section 130 may have a generally constant diameter, for example, the lowest member section 130 may be generally cylindrical in shape. However, other shapes having a substantially constant cross-sectional area may be suitable. In the illustrated embodiment, the lowest member segment 130 includes an upper tapered portion 129 at its upper end. As illustrated, this upper tapered portion 129 may extend into a bottom portion of the intermediate member section 128. The lowermost member section 130 may also include a lower tapered portion 131 at its lower end, thus promoting a more uniform flow of solid/gas mixture across the outer surface of the member 122. The lowest member section 128 may also be configured to add or remove gas from the surface interface of the solid/gas mixture. Additionally, the lowest member segment 130 may not be configured to add or remove gas from the surface interface of the solid/gas mixture. As illustrated, the lowest component section 130 may not be in communication with either the insert air inlet 112 or the insert air outlet 118.

One or more supports 132 may be provided from the flush cartridge 102 wall to the insert assembly 114 to hold it in place. As illustrated, the support 132 may also provide a channel in or below the insert assembly 114 to add or remove gas. Support 114 may further provide an area for insertion of gas inlet 112 and insertion of gas outlet 118 (which may include associated equipment such as pipes, conduits, etc. for supplying fluid communication to insertion assembly 114) to provide or remove gas from insertion assembly 114, such as by containing the associated equipment, providing support for the equipment, retaining the equipment, etc. One or more of insert air inlet 112 and/or insert air outlet 118 may also be connected to insert assembly 114 independent of one or more of supports 132. All or some of the supports, conduits, pipes, etc., including support 132, passing through the fluid zone may have a fluid-reinforced top edge, such as a knife edge, to minimize fluid disruption. For simplicity, each of insert air inlet 112 and insert air outlet 118 is also included with support 132 in fig. 1-3, but this in no way limits the orientation, placement, and selection of support 132, insert air inlet 112, and/or insert air outlet 118 that may be used in any embodiment.

The outer diameter of the member 122 may be about 75% to about 100% of the outer diameter of the reverse taper 120. Accordingly, the reverse taper 120 may have the same outer diameter as the member 122, resulting in the insert assembly 114 having a substantially constant outer diameter. The outer diameter of the member 122 may be about 75% to about 90%, or about 80% to about 90%, of the outer diameter of the reverse taper 120. The outer diameter of the member 122 may be about 80% to about 100%, or about 90% to about 100%, of the outer diameter of the reverse taper 120. Preferably, the outer diameters referred to herein are measured at points furthest apart from the referred portions, but may also refer to the median or average outer diameter thereof.

Additionally, the outer diameter of the member 122 can be about 50% to about 95% of the inner diameter of the portion of the flush cartridge 102 adjacent thereto. The outer diameter of the reverse taper 120 and/or the member 122 may be about 50% to about 95% of the inner diameter of the portion of the flush bin 102 adjacent thereto. The outer diameter of the reverse taper 120 and/or the member 122 may be about 50% to about 80%, or about 55% to about 75%, or about 60% to about 70% of the inner diameter of the portion of the flush bin 102 adjacent thereto. The outer diameter of the reverse taper 120 and/or the member 122 may be about 60% to about 95%, or about 70% to about 85%, of the inner diameter of the portion of the flush bin 102 adjacent thereto. Accordingly, there may be a relationship between the outer diameter of the member 122 and/or the reverse taper 120 and the inner diameter of the flush bin 102.

The reverse taper 120 and the component sections 126, 128, and 130 may have internal chambers, such as chambers 136, 138, 140, and 142. Each of the chambers 136, 138, 140, and 142 may or may not be in fluid communication with an adjacent one of the chambers 136, 138, 140, and 142. By way of example, the reverse taper 120 and the component sections 126, 128, and 130 may individually have upper and/or lower openings to allow fluid flow between the chambers 136, 138, 140, and 142. The openings may be in the form of, for example, tubes, sleeves, channels, or other openings to allow fluid communication between the various elements of the insert assembly 114. Embodiments of the uppermost member segment 126 may not include an opening in an upper portion thereof, and thus the chamber 136 of the inverted cone 120 is not in fluid communication with the chamber 138 of the uppermost member segment 126. Embodiments of the intermediate member segment 128 may have an opening in an upper portion thereof, and thus the chamber 140 in the intermediate member segment 128 may be in fluid communication with the chamber 138 of the uppermost member segment 126. Embodiments of the lowest member section 130 may not have openings on the upper or lower ends such that the chamber 142 may not be in fluid communication with the chamber 140 of the middle member section 128 or the flush bin 120.