Fluid treatment process and apparatus

• US 4,673,507 A
• Filed: 05/23/1985
• Issued: 06/16/1987
• Est. Priority Date: 05/06/1985
• Status: Expired due to Term

• Current Assignee: Eco-Tec Ltd.
• Original Assignee: Eco-Tec Ltd.
• Inventors: Brown, Craig J.
• Primary Examiner(s): CINTINS, IVARS C
• Application Number:
  US06/737,123
• Time in Patent Office: 754 Days
• Field of Search: 210/660, 210/681, 210/807, 210/263, 210/282, 210/289, 210/291, 210/350-353, 210/484
• US Class Current: 210/681
• CPC Class Codes: B01D 15/14 relating to the introduction of the feed to the apparatus
• CPC Class Codes: B01J 47/02 Column or bed processes
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters

Abstract

An apparatus and process for treating a fluid by passing the fluid through a bed of particulate material such as an ion exchange resin capable of taking up from the fluid a component to be removed therefrom. Substantially uniform fluid flow distribution across the cross-sectional area of the bed is achieved by employing resins of fine particle size which are maintained in an overpacked condition.

Claims

1. Apparatus for treating a fluid to remove a component therefrom, by a process in which the fluid is passed through a bed of particulate material capable of taking up the component from the fluid, wherein the apparatus comprises:

a vessel containing a said bed of particulate material, said material being an ion exchange resin that is both capable of taking up said component from the fluid and capable of being regenerated in place, and the volume of which changes appreciably in use, the vessel having first and second ports for permitting flow of fluid through the bed from said first port to said second port and reverse flow for regeneration of said resin.

means confining the bed within the vessel so that the bed defines first and second end faces, a substantially constant bed depth between said faces of less than about 30 inches, and a cross-sectional area which is constant or increases uniformly from one face to the other, said confining means including headers at the respective bed end faces, each including fluid flow passageways providing communication between the bed and the relevant one of said ports, the passageways being arranged to distribute fluid flowing from a said port into the bed substantially evenly over the cross-sectional area of the bed at said face;

said resin being fully confined by said confining means in an overpacked condition, the particle size and the degree of overpacking of said resin being selected to provide for substantially even distribution of fluid across the cross-sectional area of the bed in flowing between said bed end faces.

2. An apparatus as claimed in claim 1, wherein the particle size of the particulate material is finer than 40 U.S. mesh.

3. An apparatus as claimed in claim 2, wherein the particle size of said resin is in the range 80-120 U.S. mesh.

4. An apparatus as claimed in claim 1, wherein each said header includes a header plate formed with said fluid flow passageways, the passageways extending outwardly from a central location communicating with the relevant said port, the passageways comprising channels opening into an inner face of said plate, and a screen covering said channels and having openings smaller than the size of particles in said bed, whereby the screen prevents the resin particles entering the said passageways and the overpacked resin holds the screen against the associated header plate.

5. An apparatus as claimed in claim 4, wherein each said port comprises a tubular member extending outwardly from the relevant header plate and communicating with an opening generally centrally of said plate, the plate being provided with a baffle for preventing direct impingement on the bed of liquid flowing into the bed from said port, each said header plate being removably clamped to the vessel by a backing plate disposed outwardly of the header plate and removably secured to the vessel, the backing plate having a central opening through which said tubular member extends and the backing plate removably trapping the header plate against the vessel whereby the header plate can be removed for providing access to the bed of particulate material by removing the back plate.

6. An apparatus as claimed in claim 5, wherein the vessel comprises a open ended cylindrical member having respective flanges surrounding said open ends, and wherein the backing plates of the respective headers are removably secured to the respective flanges, trapping the associated header plates between the backing plates and said flanges.

7. An apparatus as claimed in claim 1, wherein said vessel is provided with an additional port communicating with said bed for permitting particulate resin material to be introduced into the vessel through the port for forming the bed.

8. An apparatus as claimed in claim 1, wherein the liquid hold-up volume in the flow passageways in each of the headers is less than 0.44 cubic feet per square foot of bed cross-sectional area.

9. An apparatus as claimed in claim 8, wherein said liquid hold-up volume is less than 0.03 cubic feet per square foot of bed cross-sectional area.

10. A process for treating a fluid to remove a component therefrom, in which the fluid is passed through a bed of a particulate material in the form of an ion exchange resin that is capable of both taking up the component from the fluid and of being regenerated in place and the volumne of which changes appreciably in use, wherein the bed comprises particles of substantially uniform size maintained in an overpacked condition between first and second end faces of the bed, the bed defining a substantially constant depth between said faces of less than about 30 inches and a cross-sectional area which is constant or increases uniformly from one face to the other, and wherein the fluid is passed through the bed by distributing the fluid substantially uniformly across one of said end faces, permitting the fluid to flow through the bed and collecting the fluid substantially uniformly across the other said end face, the size of the particles in the bed and the degree of overpacking being selected to provide for substantially even distribution of fluid across the cross-sectional area of the bed in flowing between said bed end faces, and the process being operated at a capacity of less than about 35% of the maximum capacity of the process.

11. A process as claimed in claim 10, wherein the particle size of the particulate material is finer than 40 U.S. mesh.

12. A process as claimed in claim 11, wherein the particle size of said material is in the range 80-120 U.S.

13. A process as claimed in claim 11, wherein said bed is of annular shape and said first and second end faces are defined by cylindrical faces at the inside and outside of the annulus, and wherein the fluid is passed through the bed by distributing the fluid across one of said cylindrical faces and collecting the fluid across the the other said cylindrical face.

14. A process as claimed in claim 10, which is operated at a approximately 12.5% of the maximum capacity of the process.

15. A process as claimed in claim 10, which is performed in a vessel having at least one removable header, confining the bed at one end face thereof, wherein the bed is formed by removing the header, overfilling the vessel with resin particles, and fitting the header to the vessel so as to compress the particles.

16. A process as claimed in claim 15, wherein the resin is caused to shrink prior to being introduced into the vessel.

17. A process as claimed in claim 10, which is performed in a vessel containing said bed of particulate material and having a port for introducing said material into the vessel, wherein the bed is formed by pumping the particulate material into the vessel through said port as a slurry in water, permitting the water in the slurry to escape from the vessel and continuing pumping until a predetermined degree of resin compression is achieved, indicating that the resin is overpacked in the vessel.

18. A process as claimed in claim 17, wherein the resin is caused to shrink prior to being introduced into the vessel.