GB2289524A - Wooden media for filtration, heat exchange or mass exchange - Google Patents

Wooden media for filtration, heat exchange or mass exchange Download PDF

Info

Publication number
GB2289524A
GB2289524A GB9409967A GB9409967A GB2289524A GB 2289524 A GB2289524 A GB 2289524A GB 9409967 A GB9409967 A GB 9409967A GB 9409967 A GB9409967 A GB 9409967A GB 2289524 A GB2289524 A GB 2289524A
Authority
GB
United Kingdom
Prior art keywords
pebbles
tank
filtration
mass
buoyant
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
GB9409967A
Other versions
GB2289524B (en
GB9409967D0 (en
Inventor
Clive Hadfield
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
WOODEN WONDERS Ltd
Original Assignee
WOODEN WONDERS Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by WOODEN WONDERS Ltd filed Critical WOODEN WONDERS Ltd
Priority to GB9409967A priority Critical patent/GB2289524B/en
Publication of GB9409967D0 publication Critical patent/GB9409967D0/en
Publication of GB2289524A publication Critical patent/GB2289524A/en
Application granted granted Critical
Publication of GB2289524B publication Critical patent/GB2289524B/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/02Loose filtering material, e.g. loose fibres
    • B01D39/04Organic material, e.g. cellulose, cotton
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/02Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath
    • B01D47/021Separating dispersed particles from gases, air or vapours by liquid as separating agent by passing the gas or air or vapour over or through a liquid bath by bubbling the gas through a liquid bath
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/14Packed scrubbers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/30Loose or shaped packing elements, e.g. Raschig rings or Berl saddles, for pouring into the apparatus for mass or heat transfer
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/06Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/30Details relating to random packing elements
    • B01J2219/302Basic shape of the elements
    • B01J2219/30215Toroid or ring
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/30Details relating to random packing elements
    • B01J2219/304Composition or microstructure of the elements
    • B01J2219/30441Wood

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Organic Chemistry (AREA)
  • Filtration Of Liquid (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

A filtration, mass exchange or heat exchange apparatus comprises a tank (2) having an inlet and an outlet and a mass of buoyant or floatable members (1, 1A, 10) in the tank. Means are provided for passing fluid through the tank and the buoyant or floatable members (1) serve as a filter and/or a contact surface for heat or mass transfer for two or more fluids. The buoyant or flexible members preferably take the form of wooden pebbles. A process for filtration and/or mass or heat exchange utilises the apparatus. Many different shapes of member are disclosed. <IMAGE>

Description

Title: APPARATUS AND PROCESS FOR FILTRATION AND HEAT OR MASS EXCHANGE The present invention relates to an apparatus and process for filtration and heat or mass exchange.
According to the present invention, there is provided a filtration, mass exchange or heat exchange apparatus comprising a tank, a plurality of buoyant or floatable members within the tank and means for passing fluid through the tank via the pebbles.
Further, according to the present invention there is provided a filtration, mass exchange or heat exchange process comprising passing fluid through a mass of buoyant or floatable members. The buoyant or floatable members are preferably wooden pebbles.
Constructional embodiments of the present invention will now be described, by way of example, with reference to the accompanying drawings, wherein: Figures 1 to 7 show cross-sections through a filter tank; and Figure 8 shows a cross-section through a mass and/or heat exchanger.
As shown in Figure 1 a mass of wooden pebbles 1 is placed in a filter tank 2.
The pebbles may be balls or ovoids. As shown in Figure 2, the pebbles 1A float at various levels when the tank 2 is filled with liquid 3. Preferably the mass comprises a plurality of larger pebbles and a plurality of smaller pebbles. In one example the largest of the largest pebbles has a radius of 2 cm and the smallest of the smaller pebbles has a radius of 1 cm measured at an equivalent point.
However, the pebbles could be larger or smaller. In this example the fluid density is 1.0 gm/cm2 and the pebble density is 0.95 gm/cm2, giving a buoyancy of 0.05 gm/cm2.
For a fluid of a particular viscosity there is a relationship between drag and fluid flow velocity. Generally the drag varies as the square of the velocity. For a particular viscosity and at particular flow rates the relationship may be as follows: Drag obtained in gm/cm2 Flow Velocity in cm/sec.
0.025 0.5 x 0.1 x 0.2 ;2x 0.4 2x A flow of x cm/sec (to be determined by experiment) establishes a drag of 0.1 gm/cm2 of projected area (A).
With a projected area (A) of pebbles of 12.6 cm2, volume (V) of 33.5 cm3, fluid density of 1.0 gm/cm3, the fluid displacement = 33.5 x 1.0 = 33.5 gm and gravity = 33.5 x 0.95 = 31.8 gm resulting in a buoyancy of 1.7 gms.
In Figure 3 filtration takes place with a down flow in which the normal direction of the flow of liquid is downwards and filtration takes place on the upper side of the mass or bed of pebbles. The larger pebbles have, for example, a volume (V) in cm3 of 33.5, a projected area (A) in cm2 of 12.6, a buoyancy effect (.05V) of 1.67, a downward drag (0. 1A) at one specific intermediate flow rate (which depends upon the viscosity of the fluid) of 1.26 and thus an upward difference of 0.41 whereas the smaller pebbles have, for example, a volume of 4.2, a projected area of 3.1, a buoyancy effect of 0.21, a downward drag at intermediate flow of 0.31 and thus a downward difference of 0.1. The differences effectively cause grading of the filter bed at the commencement of filtration. However, filtration can also take place with an up flow in which the normal direction of flow of liquid is upwards counter to gravity and filtration takes place on the underside of the mass or bed of pebbles. With down flow filtration the smaller pebbles are dragged to the bottom of the tank before the larger pebbles. A similar bed grading effect can be obtained in up flow filtration as shown in Figure 5 by choosing a pebble density slightly greater than the fluid density so that the smaller pebbles are first dragged to the top of the tank due to a bigger drag minus gravity factor. Figure 4 shows backwashing after down flow filtration. After up flow filtration as shown in Figure 6 backwashing may take place as shown in Figure 7 with a lowered liquid level and with gravity assisting cake detachment.
Figure 8 shows an embodiment of the invention for use in mass or heat exchange.
A mass 10 of wooden pebbles comprises a contact surface packing in a tank 12.
The pebbles are wholly or partially suspended in liquid 13 to form a contacting column. There is no need for physical supports and thus the flow restrictions of intermediate mechanical support is avoided. The density, size and shape of the pebbles may be varied and/or mixed to suit various applications. Liquid is sprayed into the tank 12 through inlet 14, passes down through the mass of pebbles and passes out through outlet 15. Gas or vapour enters through inlet 16, bubbles up through the mass of pebbles and passes out through outlet 17. The pebbles may also be used as a contact surface for heat or mass transfer for two or more liquids. For the purposes of mass and heat exchange other shapes and combinations of shapes of pebbles may be used. For example, the pebbles may be toroids, dumbbell-shaped or banana-shaped.
The advantages of wooden pebbles are low thermal conductivity compared to metals, so that heat loss and heat transmission may be reduced relative to metals.
By choosing appropriate species, the density of wood may be matched to particular applications. The fibrous nature of wood permits internal absorption, retention and slow release of contactants; this may be called or is like the sherrybarrel effect. Used in wooden process plant, the danger of metallic contamination of product is avoided.
Simple size grading of pebbles so that the fluid always approaches the larger interstices formed by the larger pebbles may be arranged by using a wood of slightly lower density than the fluid for downward filtration, or by using wood of a slightly higher density than the fluid for upward filtration.
The grading effect may be achieved by using pebbles of all the same density.
The effect of gravity or buoyancy varies as the volume of any one pebble. The effect of fluid drag (viscosity) varies as the projected area of the pebble. Thus in downward filtration, it is possible to achieve flow conditions in which the larger pebbles move upwards because the effect of buoyancy is greater than the downward drag. At the same condition, smaller pebbles move downward because the downward drag exceeds the buoyancy. The reverse condition may be applied to upward flow.
Small pebbles of high density and large pebbles of low density (or vice versa) can be used to enhance the effect.
Up flow filtration against the underside of wooden pebbles allows the filter medium - the pebbles - to float in the fluids, without underside support. This allows both the pebbles and the retention to be gently removed from the substrate by lowering the fluid level, which should be particularly useful for residues of large area and low density (carrot peelings, papers, etc.).

Claims (14)

1. A filtration, mass exchange or heat exchange apparatus comprising a tank, a plurality of buoyant or floatable members within the tank and means for passing fluid through the tank.
2. An apparatus according to claim 1, wherein the buoyant or floatable members take the form of wooden pebbles.
3. An apparatus according to claim 2, wherein the wooden pebbles are balls or ovoids.
4. An apparatus according to claim 3, wherein the buoyant or floatable members comprise a mass of larger pebbles and a mass of smaller pebbles.
5. An apparatus according to claim 4, wherein the largest of the larger pebbles has a radius of 2cm and the smallest of the smaller pebbles has a radius of 1cm.
6. An apparatus according to claim 2, wherein the wooden pebbles are toroids, dumbbell-shaped or banana-shaped.
7. A filtration apparatus according to any of the preceding claims, wherein the tank is provided with a fluid inlet at or adjacent to its top and with a fluid outlet at or adjacent to its bottom whereby fluid is arranged to flow through the tank in a downwards direction.
8. A filtration apparatus according to claim 7, wherein the tank is provided with a mesh screen or like support for supporting the buoyant or floatable members in the tank and for preventing said members from entering the outlet.
9. A filtration apparatus according to any one of claims 1 to 6, wherein the tank is provided with a fluid inlet at or adjacent to its bottom and with a fluid outlet at or adjacent to its top whereby fluid is arranged to flow through the tank in an upwards direction.
10. A filtration apparatus according to claim 9, wherein the tank is provided with a mesh screen or the like for preventing the buoyant or floatable members from entering the outlet.
11. A filtration, mass exchange or heat exchange apparatus substantially as described herein with reference to the drawings.
12. A filtration, mass exchange or heat exchange process comprising passing fluid through a mass of buoyant or floatable members.
13. A process according to claim 12, wherein the buoyant or floatable members take the form of wooden pebbles.
14. A filtration, mass exchange or heat exchange process substantially as described herein with reference to the drawings.
14. A process according to claim 12, wherein the buoyant or floatable members comprise the pebbles claimed in any one of claims 2 to 6.
15. A filtration, mass exchange or heat exchange process utilising the apparatus claimed in any one of claims 1 to 11.
16. A filtration, mass exchange or heat exchange process substantially as described herein with reference to the drawings.
Amendments to the claims have been filed as follows CLAIMS 1. A filtration, mass exchange or heat exchange apparatus comprising a tank, a plurality of buoyant or floatable members within the tank and means for passing fluid through the tank, wherein the buoyant or floatable members take the form of wooden pebbles.
2. An apparatus according to claim 1, wherein the wooden pebbles are balls or ovoids.
3. An apparatus according to claim 2, wherein the buoyant or floatable members comprise a mass of larger pebbles and a mass of smaller pebbles.
4. An apparatus according to claim 3, wherein the largest of the larger pebbles has a radius of 2cm and the smallest of the smaller pebbles has a radius of 1cam.
5. An apparatus according to claim 1, wherein the wooden pebbles are toroids, dumbbell-shaped or banana-shaped.
6. A filtration apparatus according to any of the preceding claims, wherein the tank is provided with a fluid inlet at or adjacent to its top and with a fluid outlet at or adjacent to its bottom whereby fluid is arranged to flow through the tank in a downwards direction.
7. A filtration apparatus according to claim 6, wherein the tank is provided with a mesh screen or like support for supporting the buoyant or floatable members in the tank and for preventing said members from entering the outlet.
8. A filtration apparatus according to any one of claims 1 to 5, wherein the tank is provided with a fluid inlet at or adjacent to its bottom and with a fluid outlet at or adjacent to its top whereby fluid is arranged to flow through the tank in an upwards direction.
9. A filtration apparatus according to claim 8, wherein the tank is provided with a mesh screen or the like for preventing the buoyant or floatable members from entering the outlet.
10. A filtration, mass exchange or heat exchange apparatus substantially as described herein with reference to the drawings.
11. A filtration, mass exchange or heat exchange process comprising passing fluid through a mass of buoyant or floatable members in the form of wooden pebbles.
12. A process according to claim 11, wherein the buoyant or floatable members comprise the pebbles claimed in any one of claims 2 to 5.
13. A filtration, mass exchange or heat exchange process utilising the apparatus claimed in any one of claims 1 to 10.
GB9409967A 1994-05-18 1994-05-18 Apparatus and proces for filtration, mass exchange or heat exchange Expired - Fee Related GB2289524B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB9409967A GB2289524B (en) 1994-05-18 1994-05-18 Apparatus and proces for filtration, mass exchange or heat exchange

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB9409967A GB2289524B (en) 1994-05-18 1994-05-18 Apparatus and proces for filtration, mass exchange or heat exchange

Publications (3)

Publication Number Publication Date
GB9409967D0 GB9409967D0 (en) 1994-07-06
GB2289524A true GB2289524A (en) 1995-11-22
GB2289524B GB2289524B (en) 1998-04-15

Family

ID=10755353

Family Applications (1)

Application Number Title Priority Date Filing Date
GB9409967A Expired - Fee Related GB2289524B (en) 1994-05-18 1994-05-18 Apparatus and proces for filtration, mass exchange or heat exchange

Country Status (1)

Country Link
GB (1) GB2289524B (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3350075A (en) * 1961-12-14 1967-10-31 Domtar Ltd Method for contacting fluids in countercurrent
GB1196814A (en) * 1968-05-22 1970-07-01 John Lillie Ramsay Kirkaldy Improvements relating to Water-Cooling Towers.
US3607741A (en) * 1970-02-19 1971-09-21 Alfred Sohnius Oil slick removal system
GB1459175A (en) * 1972-10-17 1976-12-22 Atomic Energy Authority Uk Treatment of sludges
US4582609A (en) * 1984-02-22 1986-04-15 Minnesota Mining And Manufacturing Company Filtration device and method
GB2283307A (en) * 1992-06-11 1995-05-03 Ea Tech Ltd Cold storage apparatus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3350075A (en) * 1961-12-14 1967-10-31 Domtar Ltd Method for contacting fluids in countercurrent
GB1196814A (en) * 1968-05-22 1970-07-01 John Lillie Ramsay Kirkaldy Improvements relating to Water-Cooling Towers.
US3607741A (en) * 1970-02-19 1971-09-21 Alfred Sohnius Oil slick removal system
GB1459175A (en) * 1972-10-17 1976-12-22 Atomic Energy Authority Uk Treatment of sludges
US4582609A (en) * 1984-02-22 1986-04-15 Minnesota Mining And Manufacturing Company Filtration device and method
GB2283307A (en) * 1992-06-11 1995-05-03 Ea Tech Ltd Cold storage apparatus

Also Published As

Publication number Publication date
GB2289524B (en) 1998-04-15
GB9409967D0 (en) 1994-07-06

Similar Documents

Publication Publication Date Title
US3893925A (en) Oil separator with coalescing media
US4301008A (en) Skimmer for removing the surface layer from a stretch of liquid
US4115266A (en) Method for separating foreign substances by means of a filter forming a floating layer
US4582609A (en) Filtration device and method
CA2115813A1 (en) Method and device for the separation of a contaminated top layer
GB1571637A (en) Separating oil-water mixtures
WO1999065588A1 (en) Method and apparatus for separating water from oil
CN109653177B (en) River course floating oil recovery unit
EP0119014A3 (en) Apparatus and method for physically separating a mixture of two or more liquids
US3432994A (en) Method for effecting countercurrent contacting of gas and liquid streams
CN100363093C (en) Membrane cartridge, membrane separating device, and membrane separating method
US5202031A (en) Waste water treatment system
GB2289524A (en) Wooden media for filtration, heat exchange or mass exchange
US4251369A (en) Radial design submerged coalescer for separation of liquids
US6251266B1 (en) Suction tube inlet with strainer
US4797063A (en) Floating suction apparatus
US5143618A (en) Process for the treatment of organic wastewater
JP5328749B2 (en) Apparatus and method for treating rain runoff using non-powered backwash system
CN113044903B (en) Oil-water separator
JPH0598626A (en) Effluent oil recovering method and device used therefor
US4518403A (en) Degasser-desurger unit
JP5269552B2 (en) Selective separation device for waste oil and waste water containing solids
GB2239192A (en) Filter bed
JPS5651216A (en) Separation of foreign matters by filter medium consisting of floating layer
CN213643386U (en) Utilize smart native sewage treatment plant of diatom

Legal Events

Date Code Title Description
PCNP Patent ceased through non-payment of renewal fee

Effective date: 20010518