US3618778A - Liquid-treating apparatus - Google Patents

Liquid-treating apparatus Download PDF

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US3618778A
US3618778A US3618778DA US3618778A US 3618778 A US3618778 A US 3618778A US 3618778D A US3618778D A US 3618778DA US 3618778 A US3618778 A US 3618778A
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flat
liquid
sheets
corrugations
set forth
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Joseph H Benton
Joseph A Self
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Ethyl Corp
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Ethyl Corp
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/10Packings; Fillings; Grids
    • C02F3/101Arranged-type packing, e.g. stacks, arrays
    • 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
    • B01J19/32Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • 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
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/3221Corrugated sheets
    • 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
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32213Plurality of essentially parallel sheets
    • B01J2219/3222Plurality of essentially parallel sheets with sheets having corrugations which intersect at an angle different from 90 degrees
    • 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
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32224Sheets characterised by the orientation of the sheet
    • B01J2219/32227Vertical orientation
    • 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
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322Basic shape of the elements
    • B01J2219/32203Sheets
    • B01J2219/32248Sheets comprising areas that are raised or sunken from the plane of the sheet
    • B01J2219/32251Dimples, bossages, protrusions
    • 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
    • B01J2219/32Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/324Composition or microstructure of the elements
    • B01J2219/32483Plastics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Definitions

  • a liquid-treating unit particularly suited for the treatment of liquid waste by aerobic bacterial action includes a module made of alternate flat and corrugated sheets of a l [22] Filed May 22, 1969 [45] Patented Nov. 9, 1971 73] Assignee Ethyl Corporation New York, N.Y.
  • thermoplastic material The corrugated sheets are joined to the flat sheets at the apices of the corrugations.
  • the corrugations have flat apices and reinforced sidewalls to enhance the strength of the module.
  • This invention relates to an improved module or cubeshaped filter media unit for treatment of liquids wherein the liquids are allowed to flow down over the surfaces of a series of vertically stacked modules and are contacted with a gas.
  • the module of this invention is particularly suited for use in bacterial oxidation of waste streams.
  • the corrugated sheets have been either joined at spaced apart points to the flat sheets at the peak of the crest of the corrugation or at the other edges of the sheets. This has provided some weakness in the units when subjected to high loading as occurs when the units are stacked to considerable depths, i.e., 20 feet or more without intermediate support structures or when extremely heavy biological growths are present on the large surface area provided by these types of packing units.
  • Still another object of the present invention is to provide a liquid-treating unit which can be inexpensively manufactured and readily assembled on the site, if desired.
  • a liquid-treating unit which includes a plurality of substantially flat sheets of plastic material with a sheet of plastic material having a plurality of corrugations therein positioned between adjacent sheets of the flat plastic material.
  • the corrugations are curvilinear over at least part of this length and have substantially flat apices in contact with the adjacent flat sheets.
  • Means are provided joining the flat apices of the corrugated sheets, over at least a part of their length to the flat sheets.
  • FIG. 1 is a top plan view of a corrugated sheet used in a liquid-treating unit constructed in accordance with the present invention
  • FIG. 2 is an enlarged sectional view of FIG. 1 taken along the line 2-2;
  • FIG. 3 is an enlarged sectional view of FIG. 1 taken along the line 3-3;
  • FIG. 4 is an enlarged sectional view of FIG. 1 taken along the line 4-4;
  • FIG. 5 is an enlarged sectional view of FIG. 1 taken along the line 5-5;
  • FIG. 6 is an enlarged cross-sectional view of FIG. 1 taken along the line 6-6;
  • FIG. 7 is a partial perspective view of a portion of the corrugated sheet used in the liquid-treating unit of the present invention.
  • FIG. 8 is another partial perspective view of the corrugated sheet used in the liquid treating unit of the present invention.
  • FIG. 9 is a perspective view of the flat sheet used in the liquid-treating unit of the present invention.
  • FIG. 10 is a top view of an assembled liquid-treating unit of the present invention made from alternate corrugated and flat sheets;
  • FIG. 11 is a sectional view of FIG. 10 taken along the line 1 1- 11;
  • FIG. 12 is an enlarged sectional view of FIG. 10 taken along the line 12-12;
  • FIG. 13 is an enlarged sectional view of FIG. 12 taken along the line 13-13.
  • the liquid-treating unit designated generally by the numeral 20, includes generally flat sheets 21 and alternate corrugated sheets 22.
  • the individual corrugations 23 provided in the sheet 22 are generally sinusoidal in configuration.
  • the corrugations 23 extend completely across the generally rectangular corrugated sheet 22 in the direction of its minimum dimension. It is preferred that the corrugations 23 in the corrugated sheets 22 be in the form of a truncated V in cross section.
  • This construction provides a corrugation having a generally flat apex 24.
  • the apices 24 of each of the corrugated sheets are in contact with and are attached at one or more points to the flat surface of the flat sheet 21.
  • the corrugations 23 have sidewalls 25-25 forming the sides of a truncated equilateral triangle.
  • Each sidewall 25 is provided with a plurality of reinforcing ribs 26 which extend substantially the full height of the sidewall between the adjacent flat apices 24-24.
  • the ribs 26 are provided by thermoformed, generally cylindrically shaped protrusions in the sidewall of each of the corrugations in the corrugated sheet. I-Iowever, it is understood that the ribs may take other forms.
  • each corrugated sheet is provided with a number of short length ribs 27 which extend in a direction substantially perpendicular to the length of the longer reinforcing ribs 26.
  • the corrugated sheet 22 is provided at each end with a straight end wall section 28 that does not follow the generally sinusoidal shape of the remainder of the corrugations 23 therebetween.
  • Each end wall 28 is provided with an out-turned flat terminal portion 29 at its end.
  • the straight end wall section 28 is also provided with reinforcing ribs 26 similar to those provided in the sinusoidal corrugations.
  • each alternate corrugated sheet 22 is rotated 180 so that the corrugations 23-23 in adjacent sheets are 180 out of phase.
  • this provides a plurality of contact points wherein the corrugated sheets cross over each other and provides high areas of reinforcement and rigidity for the gas-liquid contact cube when using this arrangement.
  • the invention is not limited to the arrangement wherein the alternate corrugated sheets are l out of phase. They may be all assembled with the corrugations aligned in the same direction, if so desired.
  • each flat sheet 21 has an integrally formed, generally T-shaped reinforcement bead 32 thereon.
  • the reinforcement may be produced on the longitudinally extending edges 31 of the flat sheets by clamping the assembled cube between hot upper and lower platens and applying pressure to the edges 31 of the flat sheets whereby they are fused and flattened to assume the generally T-shaped head as shown in FIG. 12 having the dimension A.
  • the provision of the reinforced edge on the flat sheets provides a wider footing whereby when cubes are stacked on one another a greater bearing surface is provided for the weight of the cube plus the weight of the biological material growing on the cubes.
  • thermoplastic liquid-treating cubes used heretofore has been the splitting of the edges of the sheets because of the high-compressive forces applied to the sharp edge of the longitudinally extending flat sheets when the cubes are stacked one on another. Additionally, as shown in FIGS. 12 and 13, the fusing of the edges 31 of the flat sheets also produces a fusion in the edge 33 of the corrugated sheet to provide a similar shaped reinforcement bead 34 having the dimension B.
  • the provision of these reinforcing beads 3434 provides a flattened area for the edge of each corrugated sheet whereby it provides a reinforced footing for contact with the adjacent cube to provide higher compressive strength. Dimensions A and B of the beads 32 and 34 may range from about one-eighth inch to about seven-sixteenths inch in width.
  • the corrugations 23 in the corrugated sheet 22 be generally in the shape of an equilateral triangle.
  • other forms such as hemispherical toroidal or any arcuate-shaped surface desired may be sued as long as the corrugations provide sufficient open space for the passage of the liquid being treated.
  • the flat sheets were 24% inches by 48% inches and the corrugated sheets were also 24% inches by 48% inches.
  • the equilateral triangle provided by the corrugation 23 in the corrugated sheet 22 has a base length of approximately 3% inches and a sidewall length of about 2% inches and the flat crest 24 pro vided at the apex of each corrugation had a width of about three-eighths inch.
  • the reinforcing rib 26 in the corrugated section of the cube projected approximately one-eighth inch above the flat sidewalls of the corrugation and had an arcuate surface having a radius of five-sixteenths inch.
  • the cube is preferably assembled by applying a solvent or a glue over the entire surface of the flat apex 24 of each of the corrugations 23 and then pressing the corrugated sheet onto a flat sheet 21. Additional corrugations are added between alternate flat sheets with glue being applied to the apices 24 of the corrugated sheets with glue being applied to the apices 24 of the corrugated sheets and also to the large flattened areas 30 adjacent each end wall corrugation of the corrugated sheets. Glue is also applied to the flat terminal portion 29 of the end walls, and this is fixed to the terminal edge of the flat sheet. The cube is then placed between heated platens and the edges fused to provide the reinforcing beads 32 and 34. This construction provides an extremely rugged cube with a very high-crush strength.
  • the sheets may be joined at spaced points by means of a radiofrequency sealer or an ultrasonic powered tool, if desired, instead of using a glue or solvent.
  • the thermoplastic used to fabricate the flat sheets and the corrugated sheets may be any rigid thermoplastic material having a suitable rigidity, i.e., preferably a Youngs modulus in the order of pounds per square inch.
  • suitable polymeric materials are polyvinyl chloride homopolymer, polyvinyl chloride copolymers, e.g., polyvinyl chloride-polyvinyl acetate copolymer, polyvinyl chloride-polyvinylidene chloride copolymer, polyvinylidene chloride homopolymer, polypropylene, high-density polyethylene, chlorinated polyvinyl chloride, chlorinated low-density polyethylene, chlorinated high-density polyethylene, polymethyl methacrylate, polystyrene, polyoxymethylene polymers and copolymers, and blends of the foregoing polymers with other polymers or copolymers.
  • Completed gas-liquid contact units described hereinbefore are stacked on top of one another in a conventional treating basin, such as one formerly used to hold rocks, with alternate layers of cubes rotated
  • the cubes of the present invention may be stacked to a height of 24 feet without additional intermediate support. They have been found to withstand very high loading when subjected to tests.
  • the material to be treated may be flowed over the stacked units in a manner used in conventional sewage treatment, i.e., rotating arms or spray nozzles.
  • reinforcing support members may be provided in the treating basin, e.g., as shown in U.S. Pat. No. 3,347,381, FIG. 10.
  • a preferred form of the liquid-treating cube of the present invention is made using homopolymer polyvinyl chloride wherein the flat sheets have a thickness of about 0.035 inch and the corrugated sheets have a thickness of about 0.025 inch (before thermoforming).
  • any reasonable wall thicknesses can be used for the thermoplastic material used to make both the flat sheets and the corrugated sheets. Sheet thicknesses of the order form 0.010 inch to as much as 0.040 inch have been found to be satisfactory for manufacturing the liquid-treating cubes of the present invention.
  • a test cube 2 feet square was made using alternating flat and thermoformed sheets as described hereinbefore from polyvinyl chloride homopolymer.
  • the flat sheets were calendered at an approximate thickness of 0.035 inch.
  • the corrugated sheets were thermoformed from flat polyvinyl chloride thermoplastic sheet material having an initial thickness of 0.025 inch.
  • the cubes were formed by gluing the corrugated sheets to the flat sheets over the entire areas of contact between the flat crests 24 of the corrugations and the areas of contact with the flat sheets.
  • the cubes were pressed against a hotplate to produce generally T-shaped flanges of about five-sixteenths inch width of opposite, longitudinally extending edges of both the flat and corrugated sheets.
  • the cubes were allowed to cure for a few days prior to being put in the test frame.
  • two cubes constructed as described above were placed in a frame with the corrugations in the same plane but with the edge surfaces of the cubes rotated 90 so the reinforced edges made contact with the ad jacent cube at the maximum number of points.
  • a load of 750 pounds per square foot was applied to the top cube and the compression of the two cubes measured.
  • the load was maintained for 3 days and no additional compression was detected.
  • the hydraulic cylinder loading the test cubes was then increased to apply a pressure of 1,060 p.s.f. to the two cubes.
  • the compression measured during this load increase indicated that the two cube had moved only three thirty-seconds of an inch additionally. No failure, i.e., no cracking, splitting, or buckling of the cubes was observed. Samples of another commercially available cube were tested and failed abruptly at 1,000 p.s.f.
  • a second test method was used for the remainder of the tests to determine the long term strength.
  • the load applied for each test was calculated from the following:
  • test load tower height X operating load X modulus decay X safety factor This corresponds to a tower design load calculated as follows:
  • the modulus decay factor used in calculating the test load results from the fact that, in a plastic, the apparent flexure modulus decays with time under load due to creep.
  • the apparent flexure modulus is calculated from the deflection of a beam of the material under load. As time under load increases, the deflection increases the calculated modulus decreases. The rate of change of modulus decreases with time so that, for rigid PVC, after about 1 year under load, the modulus has leveled out to its minimum value. Data for the decay of the apparent flexure modulus can be found in Materials Data Nomographs. by Peters, R. L.
  • the instantaneous flexure modulus for rigid PVC is 4 times that at 1 year and the 4-day value is twice that at l year.
  • the behavior after i year under load P can be determined from the behavior at 4 days under load 2? since the modulus is twice as great at 4 days as at 1 year.
  • Negligible deformation after 4 days under test load 2? implies negligible deformation after 1 year at actual load P and due to leveling out of modulus, negligible deformation for all time.
  • the 4-day test duplicates actual in-use performance.
  • the modulus decay factor is taken to be 2.5 and the safety factor is taken [.25.
  • the operating load is the sum of the weights of the module or cube and a maximum bacteria growth of l2.7
  • Table I gives design loads and test loads for various [5 conditions.
  • a liquid-treating unit in a liquid-treating unit the combination comprising: a. a plurality of substantially flat sheets of plastic material; b. a sheet of plastic material having a plurality of corruga- 0 tions therein positioned between adjacent sheets of said flat plastic material, said corrugations being curvilinear over at least a part of their length and having substantially flat apices in contact with said adjacent flat sheets, the sidewalls of said corrugations being provided with a plurality of generally arcuate -shaped reinforcing ribsand means oining said flat apices of said corrugated sheets, at
  • liquid-treating unit as set forth in claim I wherein said plastic material comprises a polyvinyl chloride 0 homopolymer.
  • each of the end corrugations in said corrugated sheet is substantially straight and provides a flat surface at its terminal end which is joined to one of said adjacent flat 5 sheets.
  • modules of the present the edges of said flat sheets and the edges of said sheets providing corrugations therein that lie in a plane perpendicular to the median line through said corrugations are of a invention that are made from 0.02S-inch-thick corrugations greater thickness than the remainder of said sheets.
  • edges are of a thickness of from about one-eighth inch to about seven-sixteenths inch.

Abstract

A liquid-treating unit particularly suited for the treatment of liquid waste by aerobic bacterial action includes a module made of alternate flat and corrugated sheets of a thermoplastic material. The corrugated sheets are joined to the flat sheets at the apices of the corrugations. The corrugations have flat apices and reinforced sidewalls to enhance the strength of the module.

Description

United States Patent I 56] Relerences Cited UNITED STATES PATENTS H1966 Renzi Inventors Joseph H. Benton;
Joseph A. Self, both oi Baton Rouge, La. Appl. No. 827,011
3,227,429 2l0/l50 X 3,232,865 2/1966 Quinn etal..... 2l0/l50X 3,347,38l l0/l967 Minch et al..... 2l0/l50X 3,402,103 9/l968 Amberg etal. 2l0/l30X Primary Examiner-Samih N. Zaharna Assistant Examiner-Charles H. Hart Attorney-Donald L. Johnson ABSTRACT: A liquid-treating unit particularly suited for the treatment of liquid waste by aerobic bacterial action includes a module made of alternate flat and corrugated sheets of a l [22] Filed May 22, 1969 [45] Patented Nov. 9, 1971 73] Assignee Ethyl Corporation New York, N.Y.
[54] LIQUID-TREATING APPARATUS 8 Claims, l3 Drawing Figs.
[52] U'.S. CL...
thermoplastic material. The corrugated sheets are joined to the flat sheets at the apices of the corrugations. The corrugations have flat apices and reinforced sidewalls to enhance the strength of the module.
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LIQUID-TREATING APPARATUS BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to an improved module or cubeshaped filter media unit for treatment of liquids wherein the liquids are allowed to flow down over the surfaces of a series of vertically stacked modules and are contacted with a gas. The module of this invention is particularly suited for use in bacterial oxidation of waste streams.
2. Description of the Prior Art Trickling filters of various types have been used heretofore for the aerobic treatment of sewage and certain types of industrial waste. The classical treatment by means of rotating arms or spray heads over a bed of rocks having a growth of aerobic bacteria thereon. In most installations air is fed from the bottom of the treating vessel to provide the oxygen for consumption by the bacteria living on the surface of the trickling filter media.
Lightweight trickling filter media made of either alternate flat and corrugated sheets or corrugated sheets of a thermoplastic material are shown in prior art U.S. Pat. Nos. 3,281,307; 3,347,381; and 3,374,994. The trickling filter units disclosed in the aforementioned patents have been commercially manufactured and installed in a number of sewage and waste treatment plants in the United States or in foreign countries. While these types of trickling filter media have been commercially successful, nevertheless, there has been found a need to provide a trickling filter unit which possesses increased strength and rigidity over those used heretofore. In trickling filter units made from thermoplastic materials available heretofore, the corrugated sheets have been either joined at spaced apart points to the flat sheets at the peak of the crest of the corrugation or at the other edges of the sheets. This has provided some weakness in the units when subjected to high loading as occurs when the units are stacked to considerable depths, i.e., 20 feet or more without intermediate support structures or when extremely heavy biological growths are present on the large surface area provided by these types of packing units.
SUMMARY OF THE INVENTION It is an object of the present invention to provide a liquidtreating unit or module which provides a large surface area for the growth of bacteria and possesses high-compressive strength.
It is another object of the present invention to provide a liquid-treating unit which is light in weight, yet has high-compressive strength.
Still another object of the present invention is to provide a liquid-treating unit which can be inexpensively manufactured and readily assembled on the site, if desired.
The foregoing objects and other advantages are provided in a liquid-treating unit which includes a plurality of substantially flat sheets of plastic material with a sheet of plastic material having a plurality of corrugations therein positioned between adjacent sheets of the flat plastic material. The corrugations are curvilinear over at least part of this length and have substantially flat apices in contact with the adjacent flat sheets. Means are provided joining the flat apices of the corrugated sheets, over at least a part of their length to the flat sheets.
Further objects and advantages will be apparent from the drawings and the following description.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a top plan view of a corrugated sheet used in a liquid-treating unit constructed in accordance with the present invention;
FIG. 2 is an enlarged sectional view of FIG. 1 taken along the line 2-2;
FIG. 3 is an enlarged sectional view of FIG. 1 taken along the line 3-3;
FIG. 4 is an enlarged sectional view of FIG. 1 taken along the line 4-4;
FIG. 5 is an enlarged sectional view of FIG. 1 taken along the line 5-5;
FIG. 6 is an enlarged cross-sectional view of FIG. 1 taken along the line 6-6;
FIG. 7 is a partial perspective view of a portion of the corrugated sheet used in the liquid-treating unit of the present invention;
FIG. 8 is another partial perspective view of the corrugated sheet used in the liquid treating unit of the present invention;
FIG. 9 is a perspective view of the flat sheet used in the liquid-treating unit of the present invention;
FIG. 10 is a top view of an assembled liquid-treating unit of the present invention made from alternate corrugated and flat sheets;
FIG. 11 is a sectional view of FIG. 10 taken along the line 1 1- 11;
FIG. 12 is an enlarged sectional view of FIG. 10 taken along the line 12-12; and
FIG. 13 is an enlarged sectional view of FIG. 12 taken along the line 13-13.
DESCRIPTION OF THE PREFERRED EMBODIMENTS Referring now to FIGS. 1 and 10, the liquid-treating unit, designated generally by the numeral 20, includes generally flat sheets 21 and alternate corrugated sheets 22. The individual corrugations 23 provided in the sheet 22 are generally sinusoidal in configuration. The corrugations 23 extend completely across the generally rectangular corrugated sheet 22 in the direction of its minimum dimension. It is preferred that the corrugations 23 in the corrugated sheets 22 be in the form of a truncated V in cross section. This construction provides a corrugation having a generally flat apex 24. As seen in FIG. 10, the apices 24 of each of the corrugated sheets are in contact with and are attached at one or more points to the flat surface of the flat sheet 21. They are preferably attached over their full length as by gluing. As can be seen more clearly in FIGS. 2-5, 7 and 8, the corrugations 23 have sidewalls 25-25 forming the sides of a truncated equilateral triangle. Each sidewall 25 is provided with a plurality of reinforcing ribs 26 which extend substantially the full height of the sidewall between the adjacent flat apices 24-24. The ribs 26 are provided by thermoformed, generally cylindrically shaped protrusions in the sidewall of each of the corrugations in the corrugated sheet. I-Iowever, it is understood that the ribs may take other forms.
As can be seen more clearly in FIGS. 3, 7 and 8, the sidewall at the edge of each corrugated sheet is provided with a number of short length ribs 27 which extend in a direction substantially perpendicular to the length of the longer reinforcing ribs 26.
As seen in FIGS. 1, 6 and 7, the corrugated sheet 22 is provided at each end with a straight end wall section 28 that does not follow the generally sinusoidal shape of the remainder of the corrugations 23 therebetween. Each end wall 28 is provided with an out-turned flat terminal portion 29 at its end. The straight end wall section 28 is also provided with reinforcing ribs 26 similar to those provided in the sinusoidal corrugations. As can be seen in FIGS. 1, 2, 7 and 8, there is provided between each straight end wall section 28 and the adjacent sinusoidal corrugation 24 a large number of generally triangular, flat areas 30 which provide a large contact area between each of the corrugated sheets and the adjacent fiat sheet.
As seen in FIG. 11, each alternate corrugated sheet 22 is rotated 180 so that the corrugations 23-23 in adjacent sheets are 180 out of phase. As pointed out in aforementioned US. Pat. No. 3,374,994, this provides a plurality of contact points wherein the corrugated sheets cross over each other and provides high areas of reinforcement and rigidity for the gas-liquid contact cube when using this arrangement. However, the invention is not limited to the arrangement wherein the alternate corrugated sheets are l out of phase. They may be all assembled with the corrugations aligned in the same direction, if so desired.
As seen in FIGS. 10, 12 and 13, the longitudinally extending edge 31 of each flat sheet 21 has an integrally formed, generally T-shaped reinforcement bead 32 thereon. The reinforcement may be produced on the longitudinally extending edges 31 of the flat sheets by clamping the assembled cube between hot upper and lower platens and applying pressure to the edges 31 of the flat sheets whereby they are fused and flattened to assume the generally T-shaped head as shown in FIG. 12 having the dimension A. The provision of the reinforced edge on the flat sheets provides a wider footing whereby when cubes are stacked on one another a greater bearing surface is provided for the weight of the cube plus the weight of the biological material growing on the cubes. It has been found that one of the causes of failure for thermoplastic liquid-treating cubes used heretofore has been the splitting of the edges of the sheets because of the high-compressive forces applied to the sharp edge of the longitudinally extending flat sheets when the cubes are stacked one on another. Additionally, as shown in FIGS. 12 and 13, the fusing of the edges 31 of the flat sheets also produces a fusion in the edge 33 of the corrugated sheet to provide a similar shaped reinforcement bead 34 having the dimension B. The provision of these reinforcing beads 3434 provides a flattened area for the edge of each corrugated sheet whereby it provides a reinforced footing for contact with the adjacent cube to provide higher compressive strength. Dimensions A and B of the beads 32 and 34 may range from about one-eighth inch to about seven-sixteenths inch in width.
As pointed out hereinbefore, it is preferred that the corrugations 23 in the corrugated sheet 22 be generally in the shape of an equilateral triangle. However, other forms such as hemispherical toroidal or any arcuate-shaped surface desired may be sued as long as the corrugations provide sufficient open space for the passage of the liquid being treated.
In one particular embodiment of the present invention, the flat sheets were 24% inches by 48% inches and the corrugated sheets were also 24% inches by 48% inches. The equilateral triangle provided by the corrugation 23 in the corrugated sheet 22 has a base length of approximately 3% inches and a sidewall length of about 2% inches and the flat crest 24 pro vided at the apex of each corrugation had a width of about three-eighths inch. The reinforcing rib 26 in the corrugated section of the cube projected approximately one-eighth inch above the flat sidewalls of the corrugation and had an arcuate surface having a radius of five-sixteenths inch.
The cube is preferably assembled by applying a solvent or a glue over the entire surface of the flat apex 24 of each of the corrugations 23 and then pressing the corrugated sheet onto a flat sheet 21. Additional corrugations are added between alternate flat sheets with glue being applied to the apices 24 of the corrugated sheets with glue being applied to the apices 24 of the corrugated sheets and also to the large flattened areas 30 adjacent each end wall corrugation of the corrugated sheets. Glue is also applied to the flat terminal portion 29 of the end walls, and this is fixed to the terminal edge of the flat sheet. The cube is then placed between heated platens and the edges fused to provide the reinforcing beads 32 and 34. This construction provides an extremely rugged cube with a very high-crush strength. The sheets may be joined at spaced points by means of a radiofrequency sealer or an ultrasonic powered tool, if desired, instead of using a glue or solvent.
The thermoplastic used to fabricate the flat sheets and the corrugated sheets may be any rigid thermoplastic material having a suitable rigidity, i.e., preferably a Youngs modulus in the order of pounds per square inch. Examples of suitable polymeric materials are polyvinyl chloride homopolymer, polyvinyl chloride copolymers, e.g., polyvinyl chloride-polyvinyl acetate copolymer, polyvinyl chloride-polyvinylidene chloride copolymer, polyvinylidene chloride homopolymer, polypropylene, high-density polyethylene, chlorinated polyvinyl chloride, chlorinated low-density polyethylene, chlorinated high-density polyethylene, polymethyl methacrylate, polystyrene, polyoxymethylene polymers and copolymers, and blends of the foregoing polymers with other polymers or copolymers.
Completed gas-liquid contact units described hereinbefore are stacked on top of one another in a conventional treating basin, such as one formerly used to hold rocks, with alternate layers of cubes rotated The cubes of the present invention may be stacked to a height of 24 feet without additional intermediate support. They have been found to withstand very high loading when subjected to tests. The material to be treated may be flowed over the stacked units in a manner used in conventional sewage treatment, i.e., rotating arms or spray nozzles. If desired, reinforcing support members may be provided in the treating basin, e.g., as shown in U.S. Pat. No. 3,347,381, FIG. 10.
A preferred form of the liquid-treating cube of the present invention is made using homopolymer polyvinyl chloride wherein the flat sheets have a thickness of about 0.035 inch and the corrugated sheets have a thickness of about 0.025 inch (before thermoforming). Depending on the strength required, i.e., the height to which the cubes are to be stacked in the treating basin, any reasonable wall thicknesses can be used for the thermoplastic material used to make both the flat sheets and the corrugated sheets. Sheet thicknesses of the order form 0.010 inch to as much as 0.040 inch have been found to be satisfactory for manufacturing the liquid-treating cubes of the present invention.
In strength tests cubes constructed in accordance with the present invention have shown superior strength compared to all other commercial thermoplastic media presently available on the market. A test cube 2 feet square was made using alternating flat and thermoformed sheets as described hereinbefore from polyvinyl chloride homopolymer. The flat sheets were calendered at an approximate thickness of 0.035 inch. The corrugated sheets were thermoformed from flat polyvinyl chloride thermoplastic sheet material having an initial thickness of 0.025 inch. The cubes were formed by gluing the corrugated sheets to the flat sheets over the entire areas of contact between the flat crests 24 of the corrugations and the areas of contact with the flat sheets. The cubes were pressed against a hotplate to produce generally T-shaped flanges of about five-sixteenths inch width of opposite, longitudinally extending edges of both the flat and corrugated sheets. The cubes were allowed to cure for a few days prior to being put in the test frame. In the first test method, two cubes constructed as described above were placed in a frame with the corrugations in the same plane but with the edge surfaces of the cubes rotated 90 so the reinforced edges made contact with the ad jacent cube at the maximum number of points. A load of 750 pounds per square foot was applied to the top cube and the compression of the two cubes measured. The cubes compressed only seven thirty-seconds of an inch under a load of 750 p.s.f. The load was maintained for 3 days and no additional compression was detected. The hydraulic cylinder loading the test cubes was then increased to apply a pressure of 1,060 p.s.f. to the two cubes. The compression measured during this load increase indicated that the two cube had moved only three thirty-seconds of an inch additionally. No failure, i.e., no cracking, splitting, or buckling of the cubes was observed. Samples of another commercially available cube were tested and failed abruptly at 1,000 p.s.f.
A second test method was used for the remainder of the tests to determine the long term strength. The load applied for each test was calculated from the following:
test load tower height X operating load X modulus decay X safety factor This corresponds to a tower design load calculated as follows:
design load tower height X operating load The modulus decay factor used in calculating the test load results from the fact that, in a plastic, the apparent flexure modulus decays with time under load due to creep. The apparent flexure modulus is calculated from the deflection of a beam of the material under load. As time under load increases, the deflection increases the calculated modulus decreases. The rate of change of modulus decreases with time so that, for rigid PVC, after about 1 year under load, the modulus has leveled out to its minimum value. Data for the decay of the apparent flexure modulus can be found in Materials Data Nomographs. by Peters, R. L. From this data, the instantaneous flexure modulus for rigid PVC is 4 times that at 1 year and the 4-day value is twice that at l year. The behavior after i year under load P can be determined from the behavior at 4 days under load 2? since the modulus is twice as great at 4 days as at 1 year. Negligible deformation after 4 days under test load 2? implies negligible deformation after 1 year at actual load P and due to leveling out of modulus, negligible deformation for all time. Thus, the 4-day test duplicates actual in-use performance. For the 4-day test load, the modulus decay factor is taken to be 2.5 and the safety factor is taken [.25. The operating load is the sum of the weights of the module or cube and a maximum bacteria growth of l2.7
lbs/cu. ft. Table I gives design loads and test loads for various [5 conditions.
One set of two cubes with 0.025-inch-thick corrugations, 0.035-inch-thick flats, and 5/l6-inch-wide edge flanges was subjected to the 4-day test with a load of 806 p.s.f., simulating a 2 l .S-foot tower. There was no damage to the cubes after the test. in an attempt to determine the instantaneous failure load, the cubes were loaded to 1,200 p.s.f. and then to L500 p.s.f. for about minutes at each load. Inspection showed no damage to the cubes. Later, these same cubes were restacked and loaded to l,500 p.s.f. for 3 days. This caused local buckling of the flat sheets below some of the crossover points. However, there was no significant blockage of the fluid flow channels. in a second attempt to determine the instantaneous failure load, the load was raised gradually to 1,900 p.s.f. No abrupt failure occurred, only an increase in bending at the crossover points.
One set of two cubes with 0.025-inch-thick corrugations, 0.025-inch-thick flats, and %-inch5/l6-inch-wide edge flanges was subjected to the 4-day test with a load of 402 p.s.f. 3 5
While the invention has been described with reference to certain specific embodiments, it will be understood that there are many variations which would fall within the true spirit of the invention.
5 What is claimed is:
l. in a liquid-treating unit the combination comprising: a. a plurality of substantially flat sheets of plastic material; b. a sheet of plastic material having a plurality of corruga- 0 tions therein positioned between adjacent sheets of said flat plastic material, said corrugations being curvilinear over at least a part of their length and having substantially flat apices in contact with said adjacent flat sheets, the sidewalls of said corrugations being provided with a plurality of generally arcuate -shaped reinforcing ribsand means oining said flat apices of said corrugated sheets, at
least over a part of their length, to said flat sheets. 2. In the liquid-treating unit as set forth in claim I wherein said plastic material comprises a polyvinyl chloride 0 homopolymer.
3. in the liquid-treating unit as set forth in claim 1 wherein the outer wall of each of the end corrugations in said corrugated sheet is substantially straight and provides a flat surface at its terminal end which is joined to one of said adjacent flat 5 sheets.
4. In the liquid-treating unit as set forth in claim I wherein the end portions of the sidewalls of each corrugation is provided with short, arcuate-shaped projections extending generally in the direction of the median line through said corrugation.
5. In the liquid-treating unit as set forth in claim 3 wherein said end corrugations each provide at least one generally triangular-shaped flat area in its flat apex.
6. In the liquid-treating unit as set forth in claim 1 wherein simulating an i l-foot tower. After 4 days at this load, there was no damage to the cubes.
As can be seen from the above tests, modules of the present the edges of said flat sheets and the edges of said sheets providing corrugations therein that lie in a plane perpendicular to the median line through said corrugations are of a invention that are made from 0.02S-inch-thick corrugations greater thickness than the remainder of said sheets.
7. In the liquid treating unit as set forth in claim 1 wherein said flat apices of said corrugated sheet are joined to said flat sheet over the full length of said apices by means of an adhesive.
8. in the liquid-treating units as set forth in claim 6 wherein said edges are of a thickness of from about one-eighth inch to about seven-sixteenths inch.
i i i 1323 UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 5, ,77 Dated N r 9, 1971 Inventor(s) Joseph H. Benton et al It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
Column 1, line 1 after "treatment" insert for the streams is to distribute the material to be treated Column 1, line 54, reads "other edges", should read outer edges Column 5, line 32, reads "sued", should read used Column 5, line 39, reads "has", should read had Column 5, line 50, after "sheets" delete with glue being; applied to the apices 2 of the corrugated sheets Column 4 line 22, reads "form", should read from Column 4, line 55, reads "cube", should read cubes Column l; line 72, reads increases the", should read increases and the Column 6, line 55, reads "units", should read unit Sirgned and sealed this 14th day of July 19 72.
(SEAL) Attest:
LDNARD l-LPLJTCIM, JR. 8.015281 GUTISCzIALK Attes ting Officer Commissioner of Patents

Claims (7)

  1. 2. In the liquid-treating unit as set forth in claim 1 wherein said plastic material comprises a polyvinyl chloride homopolymer.
  2. 3. In the liquid-treating unit as set forth in claim 1 wherein the outer wall of each of the end corrugations in said corrugated sheet is substantially straight and provides a flat surface at its terminal end which is joined to one of said adjacent flat sheets.
  3. 4. In the liquid-treating unit as set forth in claim 1 wherein the end portions of the sidewalls of each corrugation is provided with short, arcuate-shaped projections extending generally in the direction of the median line through said corrugation.
  4. 5. In the liquid-treating unit as set forth in claim 3 wherein said end corrugations each provide at least one generally triangular-shaped flat area in its flat apex.
  5. 6. In the liquid-treating unit as set forth in claim 1 wherein the edges of said flat sheets and the edges of said sheets providing corrugations therein that lie in a plane perpendicular to the median line through said corrugations are of a greater thickness than the remainder of said sheets.
  6. 7. In the liquid treating unit as set forth in claim 1 wherein said flat apices of said corrugated sheet are joined to said flat sheet over the full length of said apices by means of an adhesive.
  7. 8. In the liquid-treating units as set forth in claim 6 wherein said edges are of a thickness of from about one-eighth inch to about seven-sixteenths inch.
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US3904525A (en) * 1973-08-23 1975-09-09 Lawrence R Rosenberg Waste treatment apparatus
US3918688A (en) * 1973-04-18 1975-11-11 Sulzer Ag Static mixing device
US3951817A (en) * 1974-06-26 1976-04-20 Jet Aeration Company Sewage treatment tank and tube settler
US3952077A (en) * 1970-05-07 1976-04-20 Serck Industries Limited Liquid cooler devices
US3963810A (en) * 1973-12-20 1976-06-15 Aktiebolaget Svenska Flaktfabriken Contact body for cooling towers
DE2747769A1 (en) * 1977-10-25 1979-04-26 Mueanyagfel Dolgozo Vall Packing unit for process column or sewage purification - composed of PVC plates with undulating faces zigzag paths and hexagonal section
US4186159A (en) * 1977-05-12 1980-01-29 Sulzer Brothers Limited Packing element of foil-like material for an exchange column
US4198361A (en) * 1978-10-03 1980-04-15 Baskov Jury A Film-type rotary mass-and-heat exchange column
US4215083A (en) * 1977-04-27 1980-07-29 Richter Gedeon Vegyeszeti Gyar Rt. Packing of equipment for the purpose of contacting mainly gaseous and liquid mediums
US4225540A (en) * 1979-04-10 1980-09-30 Carl Munters-Euroform Packing for heat and material exchange, particularly for cooling towers
US4240814A (en) * 1977-08-25 1980-12-23 Ulrich Regehr Droplet separator
US4269795A (en) * 1978-03-22 1981-05-26 Wlpu Holdings Limited Packing in wet cooling towers and method of and means for supporting the packing
US4296050A (en) * 1977-05-12 1981-10-20 Sulzer Brothers Ltd. Packing element for an exchange column
US4361426A (en) * 1981-01-22 1982-11-30 Baltimore Aircoil Company, Inc. Angularly grooved corrugated fill for water cooling tower
US4518544A (en) * 1983-01-20 1985-05-21 Baltimore Aircoil Company, Inc. Serpentine film fill packing for evaporative heat and mass exchange
US4548766A (en) * 1984-05-07 1985-10-22 Marley Cooling Tower Company Vacuum formable water cooling tower film fill sheet with integral spacers
US4553993A (en) * 1983-02-19 1985-11-19 Wigley Albert F Moisture eliminator
US4579694A (en) * 1983-12-29 1986-04-01 Evapco, Inc. Wet deck fill
US4581183A (en) * 1983-12-30 1986-04-08 Engetra S.A. Packing device for an installation putting a liquid and a gas in contact
EP0190801A1 (en) * 1985-02-06 1986-08-13 Recticel A process for carrying out microbiological fermentations in a device comprising a fixed system of an open cell foam as well as a device for carrying out such processes
US4634534A (en) * 1984-09-21 1987-01-06 Bs Smogless S.P.A. Modular plastic packing for the biological treatment of waste waters by percolation
WO1987001302A1 (en) * 1985-09-05 1987-03-12 Min Alexander Hsia Tower packing element
US4670196A (en) * 1985-09-05 1987-06-02 Norton Company Tower packing element
US4675103A (en) * 1985-12-17 1987-06-23 Hungaria Muanyagfeldolgozo Vallalat Film-flow packing for biological treatment of fluids
US4929399A (en) * 1988-03-17 1990-05-29 Union Carbide Industrial Gases Technology Inc. Structured column packing with liquid holdup
US5389248A (en) * 1993-05-21 1995-02-14 Bioremetek, Inc. Bioreactor for biological treatment of contaminated water
US5454988A (en) * 1994-01-12 1995-10-03 Mitsubishi Corporation Packing to be used in substance and/or heat exchanging tower
US5545327A (en) * 1994-06-15 1996-08-13 Smith & Loveless, Inc. Wastewater treatment method and apparatus
US5616289A (en) * 1994-01-12 1997-04-01 Mitsubishi Corporation Substance and/or heat exchanging tower
US6206350B1 (en) 1998-11-25 2001-03-27 Baltimore Aircoil Company, Inc. Film fill-pack for inducement of spiraling gas flow in heat and mass transfer contact apparatus with self spacing fill-sheets
US6260830B1 (en) 1998-11-25 2001-07-17 Baltimore Aircoil Company, Inc. Film fill-pack for inducement of spiraling gas flow in heat and mass transfer contact apparatus with self-spacing fill-sheets
US6422738B2 (en) * 1998-09-25 2002-07-23 Man Nutzfahrzeuge Ag Compact cross-channel mixer
EP1310299A2 (en) * 2001-11-13 2003-05-14 J.A. Niemeijer B.V. Structured packing material and biological cleaners provided with such a structured packing material
US20050137087A1 (en) * 2002-08-02 2005-06-23 Emitec Gesellschaft Fur Emissionstechnologie Mbh Metallic layer with regions of varying material thickness, method for producing such a metallic layer and honeycomb body at least partly produced from such metallic layers
US20060001182A1 (en) * 2004-06-30 2006-01-05 Marley Cooling Technologies, Inc. Cooling tower film fill apparatus and method
WO2006003026A1 (en) * 2004-07-07 2006-01-12 National University Of Ireland, Galway A biofilm reactor
EP1719738A1 (en) * 2005-05-04 2006-11-08 Epur S.A. Cartridge comprising a fixed bed for use in sewage treatment plants
US20080093294A1 (en) * 2006-10-20 2008-04-24 Brentwood Industries, Inc. Biological treatment system and assembly
EP2027902A1 (en) * 2007-08-22 2009-02-25 Swantje Mignon Schlederer Sedimentation tank for sewage treatment plants
KR100929373B1 (en) 2007-10-09 2009-12-02 주식회사 경인기계 Cooling tower filler
WO2010063940A1 (en) * 2008-12-04 2010-06-10 L'Air Liquide, Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude Method and device for manufacturing a structured lining wave, and such a lining wave
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Publication number Priority date Publication date Assignee Title
US3952077A (en) * 1970-05-07 1976-04-20 Serck Industries Limited Liquid cooler devices
US3918688A (en) * 1973-04-18 1975-11-11 Sulzer Ag Static mixing device
US3904525A (en) * 1973-08-23 1975-09-09 Lawrence R Rosenberg Waste treatment apparatus
US3963810A (en) * 1973-12-20 1976-06-15 Aktiebolaget Svenska Flaktfabriken Contact body for cooling towers
US3951817A (en) * 1974-06-26 1976-04-20 Jet Aeration Company Sewage treatment tank and tube settler
US4215083A (en) * 1977-04-27 1980-07-29 Richter Gedeon Vegyeszeti Gyar Rt. Packing of equipment for the purpose of contacting mainly gaseous and liquid mediums
US4186159A (en) * 1977-05-12 1980-01-29 Sulzer Brothers Limited Packing element of foil-like material for an exchange column
US4296050A (en) * 1977-05-12 1981-10-20 Sulzer Brothers Ltd. Packing element for an exchange column
US4240814A (en) * 1977-08-25 1980-12-23 Ulrich Regehr Droplet separator
DE2747769A1 (en) * 1977-10-25 1979-04-26 Mueanyagfel Dolgozo Vall Packing unit for process column or sewage purification - composed of PVC plates with undulating faces zigzag paths and hexagonal section
US4269795A (en) * 1978-03-22 1981-05-26 Wlpu Holdings Limited Packing in wet cooling towers and method of and means for supporting the packing
US4198361A (en) * 1978-10-03 1980-04-15 Baskov Jury A Film-type rotary mass-and-heat exchange column
US4225540A (en) * 1979-04-10 1980-09-30 Carl Munters-Euroform Packing for heat and material exchange, particularly for cooling towers
US4361426A (en) * 1981-01-22 1982-11-30 Baltimore Aircoil Company, Inc. Angularly grooved corrugated fill for water cooling tower
US4518544A (en) * 1983-01-20 1985-05-21 Baltimore Aircoil Company, Inc. Serpentine film fill packing for evaporative heat and mass exchange
US4553993A (en) * 1983-02-19 1985-11-19 Wigley Albert F Moisture eliminator
US4579693A (en) * 1983-02-19 1986-04-01 Wigley Albert F Liquid/gas contact means
US4579694A (en) * 1983-12-29 1986-04-01 Evapco, Inc. Wet deck fill
US4668321A (en) * 1983-12-30 1987-05-26 Engetra, S.A. Method of manufacturing a packing device for an installation putting a liquid and a gas in contact
US4581183A (en) * 1983-12-30 1986-04-08 Engetra S.A. Packing device for an installation putting a liquid and a gas in contact
EP0163911A2 (en) * 1984-05-07 1985-12-11 The Marley Cooling Tower Company Vacuum formable water cooling tower film fill sheet with integral spacers
EP0163911A3 (en) * 1984-05-07 1986-09-10 The Marley Cooling Tower Company Vacuum formable water cooling tower film fill sheet with integral spacers
US4548766A (en) * 1984-05-07 1985-10-22 Marley Cooling Tower Company Vacuum formable water cooling tower film fill sheet with integral spacers
US4634534A (en) * 1984-09-21 1987-01-06 Bs Smogless S.P.A. Modular plastic packing for the biological treatment of waste waters by percolation
EP0190801A1 (en) * 1985-02-06 1986-08-13 Recticel A process for carrying out microbiological fermentations in a device comprising a fixed system of an open cell foam as well as a device for carrying out such processes
WO1987001302A1 (en) * 1985-09-05 1987-03-12 Min Alexander Hsia Tower packing element
US4670196A (en) * 1985-09-05 1987-06-02 Norton Company Tower packing element
US4675103A (en) * 1985-12-17 1987-06-23 Hungaria Muanyagfeldolgozo Vallalat Film-flow packing for biological treatment of fluids
US4929399A (en) * 1988-03-17 1990-05-29 Union Carbide Industrial Gases Technology Inc. Structured column packing with liquid holdup
US5389248A (en) * 1993-05-21 1995-02-14 Bioremetek, Inc. Bioreactor for biological treatment of contaminated water
US5454988A (en) * 1994-01-12 1995-10-03 Mitsubishi Corporation Packing to be used in substance and/or heat exchanging tower
US5616289A (en) * 1994-01-12 1997-04-01 Mitsubishi Corporation Substance and/or heat exchanging tower
US5545327A (en) * 1994-06-15 1996-08-13 Smith & Loveless, Inc. Wastewater treatment method and apparatus
US6422738B2 (en) * 1998-09-25 2002-07-23 Man Nutzfahrzeuge Ag Compact cross-channel mixer
US6206350B1 (en) 1998-11-25 2001-03-27 Baltimore Aircoil Company, Inc. Film fill-pack for inducement of spiraling gas flow in heat and mass transfer contact apparatus with self spacing fill-sheets
US6260830B1 (en) 1998-11-25 2001-07-17 Baltimore Aircoil Company, Inc. Film fill-pack for inducement of spiraling gas flow in heat and mass transfer contact apparatus with self-spacing fill-sheets
EP1310299A2 (en) * 2001-11-13 2003-05-14 J.A. Niemeijer B.V. Structured packing material and biological cleaners provided with such a structured packing material
EP1310299A3 (en) * 2001-11-13 2006-07-05 J.A. Niemeijer B.V. Structured packing material and biological cleaners provided with such a structured packing material
US20050137087A1 (en) * 2002-08-02 2005-06-23 Emitec Gesellschaft Fur Emissionstechnologie Mbh Metallic layer with regions of varying material thickness, method for producing such a metallic layer and honeycomb body at least partly produced from such metallic layers
US7011893B2 (en) * 2002-08-02 2006-03-14 Emitec Gesellschaft Fuer Emissionstechnologie Mbh Metallic layer with regions of varying material thickness, method for producing such a metallic layer and honeycomb body at least partly produced from such metallic layers
US7237769B2 (en) * 2004-06-30 2007-07-03 Spx Cooling Technologies, Inc. Cooling tower film fill apparatus and method
US20060001182A1 (en) * 2004-06-30 2006-01-05 Marley Cooling Technologies, Inc. Cooling tower film fill apparatus and method
US7938965B2 (en) * 2004-07-07 2011-05-10 National University Of Ireland Biofilm reactor
US20090152195A1 (en) * 2004-07-07 2009-06-18 Michael Rodgers Biofilm reactor
WO2006003026A1 (en) * 2004-07-07 2006-01-12 National University Of Ireland, Galway A biofilm reactor
EP1719738A1 (en) * 2005-05-04 2006-11-08 Epur S.A. Cartridge comprising a fixed bed for use in sewage treatment plants
US20080093294A1 (en) * 2006-10-20 2008-04-24 Brentwood Industries, Inc. Biological treatment system and assembly
US7491325B2 (en) * 2006-10-20 2009-02-17 Brentwood Industries, Inc. Biological treatment system and assembly
US20110127205A1 (en) * 2007-08-22 2011-06-02 Swantje Mignon Schlederer Sedimentation basin for sewage treatment plants
WO2009024606A1 (en) * 2007-08-22 2009-02-26 Swantje Mignon Schlederer Sedimentation basin for sewage treatment plants
EP2027902A1 (en) * 2007-08-22 2009-02-25 Swantje Mignon Schlederer Sedimentation tank for sewage treatment plants
KR100929373B1 (en) 2007-10-09 2009-12-02 주식회사 경인기계 Cooling tower filler
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