US3468103A - Method and apparatus for corrosion prevention - Google Patents
Method and apparatus for corrosion prevention Download PDFInfo
- Publication number
- US3468103A US3468103A US597493A US3468103DA US3468103A US 3468103 A US3468103 A US 3468103A US 597493 A US597493 A US 597493A US 3468103D A US3468103D A US 3468103DA US 3468103 A US3468103 A US 3468103A
- Authority
- US
- United States
- Prior art keywords
- air
- container
- conduit
- moisture
- drying
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title description 24
- 238000005536 corrosion prevention Methods 0.000 title description 5
- 238000001035 drying Methods 0.000 description 57
- 238000010438 heat treatment Methods 0.000 description 25
- 239000002274 desiccant Substances 0.000 description 21
- 239000002250 absorbent Substances 0.000 description 20
- 239000007788 liquid Substances 0.000 description 16
- 239000000463 material Substances 0.000 description 8
- 230000008929 regeneration Effects 0.000 description 8
- 238000011069 regeneration method Methods 0.000 description 8
- 230000001172 regenerating effect Effects 0.000 description 6
- 238000005260 corrosion Methods 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 5
- 230000000717 retained effect Effects 0.000 description 5
- 238000005429 filling process Methods 0.000 description 4
- 230000004044 response Effects 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 238000007605 air drying Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 239000000741 silica gel Substances 0.000 description 3
- 229910002027 silica gel Inorganic materials 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000035900 sweating Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
- 238000011179 visual inspection Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
- F26B21/083—Humidity by using sorbent or hygroscopic materials, e.g. chemical substances, molecular sieves
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
- B65D90/00—Component parts, details or accessories for large containers
- B65D90/22—Safety features
Definitions
- a receptacle defines an enclosed space and contains a confined body of gaseous desiccant. Means is provided for admitting into the enclosed space a liquid containing an evaporable fraction, and for showering such liquid through the body of gaseous desiccant whereby at least a portion of the evaporable fraction is retained in the gaseous desiccant which becomes enriched therewith.
- a container containing a quantity of an additional desiccant is arranged adjacent the receptacle, and means is provided which is associated with both the receptacle and the container and is operative for at least intermittently passing the enriched gaseous desiccant from the enclosed space of the receptacle into contact with the additional desiccant in the container to thereby withdraw the retained evaporable fraction from the gaseous desiccant and to regenerate the latter.
- the present invention relates to a maintenance-free method for preventing the internal corrosion of closed transport and/ or storage containers, particularly of above ground containers for heating oil.
- the invention also relates to an apparatus for carrying out the method.
- a maintenance-free method of this type, and the necessary apparatus therefor, are needed because the internal corrosion, particularly of above-ground heating oil containers, or the like, must be prevented not only because of the losses resulting therefrom in terms of damaged containers and lost contents, but also because of the danger of ground water contamination.
- the requirement for the method and the apparatus to be maintenance free is particularly urgent because the supervision of such installations cannot be expected of private persons and because, on the other hand, the replacement of the drying medium in air drying installations becomes too expensive in the long run.
- a more specific object of the invention is to provide a method of removing from the interior of a closed container such moisture as has been imported thereinto with the material to be stored in the container.
- An additional object of the invention is to provide such a method which assures a satisfactory, reliable and maintenance-free operation of a drying arrangement without the need for constant exchange of a drying medium.
- a concomitant object of the invention is to provide an apparatus for carrying out the method.
- I provide a maintenance-free method for drying air in which an absorbing medium contained in a drying zone associated with a container is regenerated within the drying apparatus before and/or during filling of the container. Furthermore, the air escaping from the container during filling of the latter serves as carrier for conveying moisture which is freed during such regeneration and for carrying such moisture to the exterior of the container. Additionally, my novel method provides for returning material, which has been withdrawn from the container in excess of the required quantity, in finely distributed state into the actively hygroscopic air space existing above the container contents and filled with dry air, and for circulating the air content in the space above the contents of the container over or through a drying medium.
- the method it is contemplated to directly or indirectly trigger the regeneration of the absorbing medium via the material to be stored and/or the actual filling process.
- This can be achieved by utilizing the air escaping from the container during the filling process for directly or indirectly raising the temperature of the absorbing medium to the regeneration level, and for utilizing the escaping air, which as a result of the temperature raise has become hygroscopically activated, for absorbing the moisture freed during regeneration and for carrying this moisture to the exterior of the container.
- An apparatus for carrying out the method includes a drying apparatus arranged to contain an absorbing medium and constructed to simultaneously serve as a regenerating apparatus.
- Such drying apparatus is provided with a source of heat which is controlled by suitable switching means in such a manner that the source of heat is switched on upon the escape of air during filling of the container and is switched oif upon the entry of air during the withdrawal of the contents of the container.
- the air space existing above the contents of the container be connected with the drying apparatus via a circulating conduit so that moisture imported into the container by the contents can again be removed from the air.
- the invention further contemplates to provide the absorbing medium in several superposed chambers in which the medium is loosely layered and whose bottoms consist of sieve-type electrical heating grids.
- An electrical switching arrangement is provided in form of a flowswitch and arranged in the filling conduit, and this switch is associated with a safety switch which is actuated directly or indirectly by a closure provided in the inlet conduit.
- FIG. 1 is a schematic illustration of a fully automated apparatus for carrying out the method in accordance with the present invention
- FIG. 2 is a vertical longitudinal section through a drying and regenerating apparatus in accordance with the present invention
- FIG. 3 is a longitudinal section through the inlet of a filling conduit and through a closure means provided therefor;
- FIG. 4 is a transverse section through the arrangement shown in FIG. 3.
- the maintenance-free method for preventing interior corrosion of closed storage and/ or transport containers comprises the following stages:
- the air which enters the container during Withdrawal of the contents therefrom is freed from its moisture content in a known manner by passage through a drying zone filled with an absorbing medium such as silica gel or the like. This air enters in dried condition into the container and fills the space existing above the contents.
- the air above the contents of the container which now is saturated or enriched with the moisture yielded by the contents, is caused to pass through the drying zone in the ventilating conduit and is returned to the storage container in dried condition.
- the air in the container is exhausted to the exterior via the ventilating conduit during filling of the container. On its way, it is heated upstream of and/or within the drying zone by passage through a heating zone to a level above the expelling or regenerating temperature, that is to 140200 C. if silica gel is used as absorbing medium, and this air thus expels the moisture previously absorbed by the absorbing medium.
- the air which has become strongly hygroscopic as a result of its heating, absorbs the thus expelled moisture and carries it to the exterior of the container.
- heating of the heating zone is interrupted and the process repeats itself when withdrawal of material from the container again commences.
- the individual stages namely drying, regenerating and moisture removal, assure maintenance-free operation for preventing internal corrosion resulting from sweating and moisture transfer.
- FIG. 1 shows an apparatus for carrying out the method incorporated, by way of example, in a heating-oil storage installation.
- the apparatus shown in FIG. 1 comprises an aboveground heating-oil storage container 1 comprising a ventilating conduit 2 which incorporates a drying apparatus 3.
- This drying apparatus 3 is connected via an air-circulating conduit 4 with the air space 5 above the heating-oil 6 in the container 1.
- a filling conduit 7 is provided with electrical switches 8 and 9, of which the switch 8 is constructed as a flow-switch whereas switch 9 is a lever-type interrupter.
- Switch 9 is operatively connected, as will be seen in FIG. 3, with a closure arrangement 23 of the filling conduit 7.
- the container 1 further comprises a withdrawal conduit 11 and a retum-flow conduit 12 and is connected with the pump 13 of an oil burner.
- the return-flow conduit 12 communicates at the upper edge of the container 1 in the air space 5 with a distributor tube 14.
- switches 8 and 9 are connected in series in a circuit which leads to a heating chamber 15 arranged below the drying apparatus 3, and in which chamber there is provided an electrical flowthrough heater 16.
- the drying apparatus 3 of FIG. 1 consists, as shown in FIG. 2, of a cylindrical housing portion 3a whose two ends are respectively closed oif with a convex bottom .4 member 3b, 3c.
- the bottom members 3! and 3c are provided with threaded tubular extensions 3d which serve for connecting the apparatus with the ventilating conduit 2a.
- the bottom members 3!; and 3c and the housing portion 3a are provided with end faces 3e which serve to center the elements relative to one another during assembly.
- the bottom members 3b and 3c are connected to the housing portion 3a by means of a suitable clamping member 3
- the lower end of the housing portion 3 is provided in the interior thereof with a radially inwardly extending annular flange 3g which serves to support the lower plates 17 of a carrier 18 which at its upper end is provided with a handle 18a.
- Several sieve-type plates 17 are secured to the carrier 18 vertically spaced from one another so as to receive the drying medium 19, e.g. silica gel.
- the spacing between the individual plates 17 is so selected that the space 20 existing above the loosely dispersed drying medium 19 has a volume which is substantially the same, or greater than, the volume of the drying medium 19.
- a tubular outlet portion 4b is provided in the wall of the housing portion 3a below the second plate 17 and serves for connection of the aircirculating conduit 4.
- the height to which the drying medium 19 is poured onto the plate 17 above the tubular outlet portion 4b is so selected that gas pressure which might develop in the air-circulating conduit 4 encounters resistance of such magnitude as to assure that the infiowing air must flow downwardly to the ventilating conduit 2 and through the same into the container 1 (FIG. 1), and that it cannot instead escape to the exterior through the ventilating conduit 2a.
- a one-Way valve 4a (FIG. 1) is provided in the aircirculating conduit 4 and prevents the air which is displaced during filling of the container via the filling conduit 7 from returning into the container 1 through the air-circulating conduit 4.
- An electric flowthrough heater 16 is provided in the bottom member 312 and may consist of a ceramic plate 16b provided with bores 16a and with spiral grooves in which a heating coil is arranged in a known manner.
- the wall of the housing of drying apparatus 3 can be provided with viewing apertures for permitting visual control of the degree to which the drying medium is saturated so that, if an absorbing medium with a c0lorchange indicating function is utilized, for example from blue to pink, it can be readily determined by visual inspection whether the drying medium is still performing its drying function.
- a heating chamber 15 is provided below the spaces 19, 20 for the drying medium, and it is this chamber in which the heating element 16c is arranged so as to constitute therewith a flowthrough heater 16.
- the electrical connections of heating element 160 pass through suitable insulators to the exterior of the apparatus shown in FIG. 2 and are connected with a source of electrical energy via the switches 8 and 9 which, as indicated in FIG. 1, are connected in series.
- the electrical flowthrough heater 16 it is also possible to constitute the plates 17 as electrical heating grids. In any case, it is advantageous to select the volume of the free spaces 20 so large that the volume of air in the drying apparatus 3 is equal to or greater than the volume of air which flows into the oil container 1 in compensation for the withdrawal of heating-oil by the oil burner during operation of the same for a period of one hour.
- FIGS. 3 and 4 The electrical control arrangement for the flow-through heater 16 is shown in FIGS. 3 and 4 in a single exemplary embodiment.
- the filling conduit 7 which is provided with an aperture 7a through which latter an actuating lever 8a of a flow-switch 8, which latter is secured to the conduit 7 at the exterior thereof, extends into the interior of the conduit 7 and thus into the path of material flowing therethrough.
- the flow-switch 8 is constructed, in this embodiment, as a microswitch.
- the end portion of the conduit 7 is provided with an exterior grid 22 which meshes with a complementary thread provided on a cap or similar member 23 for closing the conduit 7.
- the cap 23 is provided with a tubular extension 23a which extends into the open end of the conduit 7 and which, in the mated condition of the above-mentioned threads, engages and deflects the switching lever 9a of a safety switch 9 which is also provided at the exterior surface of the conduit 7 in such a manner that the switching lever 9a extends through a second aperture 7b into the interior of the conduit 7 and can be engaged by the tubular extension 23a.
- air is aspirated into the container 1 through the ventilating conduit 2a, 2.
- this air is aspirated from the drying apparatus 3 where its inherent moisture content has been removed by the relatively long contact with the drying medium 19 contained loosely in the several chambers 20. This moisture was absorbed by the drying medium 19.
- the dry air aspirated from the drying apparatus 3 is followed by moisture-containing exterior air which enters through the ventilating conduit 2a and flows through the drying apparatus 3 at considerably reduced speed during which passage it is relieved of its moisture by absorption of the same through the drying medium 19.
- the air above the heating oil 6 is withdrawn through the air-circulating conduit 4 by means of a suitable pump and is returned to the air space 5 of the container 1 via the one-way valve 4a and the drying apparatus where it is subjected to a drying action.
- This heated air in turn heats the drying medium 19 contained in the drying apparatus 3 to the necesasry regencrating temperature and thus expels the moisture absorbed in the drying medium.
- Heating of the dry air results in hygroscopic activation of the same which in turn causes an accelerated absorption of the moisture expelled from the drying medium 19 which is carried by the air to the exterior of the container through the ventilating conduit 2a.
- the ventilating conduit 2a is protected against the entry of rain or the like by a cap 2b which is open in downward direction.
- the speed of the displaced air is relatively high so that the drying medium 19 disposed on the plates 17 is lifted by the air flow. This results not only in a reduction in the How resistance and an unhindered movement of the air, but also and primarily in a good contact of the air with the individual particles of drying medium 19 so that the warm regenerating air flows intimately about the surfaces of the individual particles, thereby assuring a rapid and complete regeneration of the drying medium 19.
- a conduit 21 with a two-pole manually operable switch 22. Actuation of the switch 22 then will turn on a blower as well as the heater 16, so that, as described above, an intermediate regeneration of the drying medium by means of heated air is accomplished. Since the drying apparatus is provided with a removable hood, the drying medium itself can be easily replaced at any time. It is simply necessary to remove the clamp 31 and to separate one of the two bottoms 3b or 3c from the cylindrical housing portion 3a to such an extent that the latter can be laterally withdrawn.
- a method of corrosion prevention comprising the steps of confining in an enclosed space a body of moisture-absorbent gaseous medium; admitting into said enclosed space and showering through said moisture-absorbent gaseous medium a quantity of liquid containing an evaporable corrosion-promoting fraction, whereby said moisture-absorbent gaseous medium retains at least a portion of said fraction and becomes enriched therewith; intermittently circulating the thus enriched moisture-absorbent gaseous medium into contact with a desiccant so as to withdraw the retained evaporable fraction and entrap the same in said desiccant; and intermittently admitting additional quantities of said liquid into said enclosed space so as to expel some of the enriched moistureabsorbent gaseous medium from said enclosed space and at such times regenerating said desiccant in response to such admission of additional quantities of said liquid to thereby expel the entrapped evaporable fraction from said desiccant.
- said enclosed space additionally contains a body of said liquid; and further comprising the step of withdrawing liquid from said body of liquid at a rate in excess of the rate at which liquid containing said evaporable fraction is admitted into said enclosed space.
- An arrangement of the character described comprising, in combination, a receptacle defining an enclosed space and containing a confined body of moisture-absorbent gaseous medium; first supply means operatively associated with said receptacle and arranged for admitting into said enclosed space a liquid containing an evaporable fraction, and for showering said liquid through said body of moisture-absorbent gaseous medium whereby at least a portion of said fraction is retained in said moisture-absorbent gaseous medium, which latter is enriched thereby; second supply means associated with said receptacle and operative for supplying additional liquid containing evaporable fraction thereinto to compress said body of moisture-absorbent gaseous medium and expel some of the enriched moisture-absorbent gaseous medium from said receptacle in response to admittance of such additional liquid; container means containing a quantity of desiccant; and means associated with said receptacle and said container means and being operative for intermittently circulating the enriched moisture-
- said container means comprises peripheral wall means defining a chamber communicating with the atmosphere; and divider wall means defining a chamber and divider wall means dividing said chamber into a plurality of chambers each of which contains some of said desiccant.
- said container means further comprises support means arranged within said peripheral wall means, said divider wall means being mounted on said support means for removal from the confines of said peripheral wall means.
- said moisture-absorbent gaseous medium is dry air; further comprising a user device associated with said receptacle and adapted to at least intermittently withdraw some of said liquid therefrom, resulting in automatic aspiration of additional air from said chamber and into said receptacle through said first conduit means; and wherein said chamber has a volumetric capacity so selected as to contain a quantity of air at least equal to the amount of additional air aspirated into said receptacle during operation of said user device for a predetermined interval.
- heating means comprises electric heating grids provided on said divider wall means.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Drying Of Gases (AREA)
- Drying Of Solid Materials (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DEH57805A DE1265535B (de) | 1965-11-29 | 1965-11-29 | Wartungsfreies Verfahren und Einrichtung zur Verhinderung der Innenkorrosion an Lagerbehaeltern, insbesondere fuer die Heizoellagerung |
Publications (1)
Publication Number | Publication Date |
---|---|
US3468103A true US3468103A (en) | 1969-09-23 |
Family
ID=7159894
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US597493A Expired - Lifetime US3468103A (en) | 1965-11-29 | 1966-11-28 | Method and apparatus for corrosion prevention |
Country Status (5)
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3543482A (en) * | 1967-05-01 | 1970-12-01 | W D Gale Inc | Air drier system |
US3628758A (en) * | 1969-07-22 | 1971-12-21 | Parker Hannifin Corp | Fuel tank inerting system |
US4218224A (en) * | 1975-12-12 | 1980-08-19 | The Dow Chemical Company | Method for controlling the regeneration and desorbtion of an absorbent material |
US5198001A (en) * | 1991-09-13 | 1993-03-30 | Calgon Carbon Corporation | Apparatus and process for removing organic compounds from a gas stream |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2340898A (en) * | 1941-11-29 | 1944-02-08 | Gen Electric | Electric apparatus |
US2569537A (en) * | 1950-03-15 | 1951-10-02 | Specialties Inc | Humidity control unit |
US2584889A (en) * | 1943-09-10 | 1952-02-05 | Merlin Gerin | Device for preventing humidity in enclosures containing insulating parts |
US2586670A (en) * | 1945-01-31 | 1952-02-19 | Christian J Lambertsen | Selective gas adsorber |
US2976950A (en) * | 1958-01-17 | 1961-03-28 | Oscar C Smith | Method and apparatus for preventing moisture accumulation in tanks |
US3193985A (en) * | 1960-07-11 | 1965-07-13 | Atlantic Res Corp | Method and apparatus for dehumidification of gases |
US3320724A (en) * | 1964-08-24 | 1967-05-23 | Comstock & Wescott | Heat-storage breather system |
-
1965
- 1965-11-29 DE DEH57805A patent/DE1265535B/de active Pending
-
1966
- 1966-11-11 CH CH1629366A patent/CH492803A/de not_active IP Right Cessation
- 1966-11-25 AT AT1092666A patent/AT276896B/de not_active IP Right Cessation
- 1966-11-28 US US597493A patent/US3468103A/en not_active Expired - Lifetime
- 1966-11-29 BE BE690403D patent/BE690403A/xx unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2340898A (en) * | 1941-11-29 | 1944-02-08 | Gen Electric | Electric apparatus |
US2584889A (en) * | 1943-09-10 | 1952-02-05 | Merlin Gerin | Device for preventing humidity in enclosures containing insulating parts |
US2586670A (en) * | 1945-01-31 | 1952-02-19 | Christian J Lambertsen | Selective gas adsorber |
US2569537A (en) * | 1950-03-15 | 1951-10-02 | Specialties Inc | Humidity control unit |
US2976950A (en) * | 1958-01-17 | 1961-03-28 | Oscar C Smith | Method and apparatus for preventing moisture accumulation in tanks |
US3193985A (en) * | 1960-07-11 | 1965-07-13 | Atlantic Res Corp | Method and apparatus for dehumidification of gases |
US3320724A (en) * | 1964-08-24 | 1967-05-23 | Comstock & Wescott | Heat-storage breather system |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3543482A (en) * | 1967-05-01 | 1970-12-01 | W D Gale Inc | Air drier system |
US3628758A (en) * | 1969-07-22 | 1971-12-21 | Parker Hannifin Corp | Fuel tank inerting system |
US4218224A (en) * | 1975-12-12 | 1980-08-19 | The Dow Chemical Company | Method for controlling the regeneration and desorbtion of an absorbent material |
US5198001A (en) * | 1991-09-13 | 1993-03-30 | Calgon Carbon Corporation | Apparatus and process for removing organic compounds from a gas stream |
Also Published As
Publication number | Publication date |
---|---|
DE1265535B (de) | 1968-04-04 |
BE690403A (GUID-C5D7CC26-194C-43D0-91A1-9AE8C70A9BFF.html) | 1967-05-02 |
AT276896B (de) | 1969-12-10 |
CH492803A (de) | 1970-06-30 |
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