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Publication numberUS3010216 A
Publication typeGrant
Publication dateNov 28, 1961
Filing dateNov 15, 1957
Priority dateNov 17, 1956
Publication numberUS 3010216 A, US 3010216A, US-A-3010216, US3010216 A, US3010216A
InventorsHeinz Ravet
Original AssigneeNat Res Corp
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Apparatus for drying heat sensitive products
US 3010216 A
Abstract  available in
Previous page
Next page
Claims  available in
Description  (OCR text may contain errors)

H. RAVET 3,010,216

APPARATUS FOR DRYING HEAT SENSITIVE PRODUCTS Nov. 28, 1961 Filed Nov. 15, 1957 INVENTOR. Huh 2' H d United States Patent Ofiice 3,010,216 Patented Nov. 28, 1961 3,010,216 APPARATUS FOR DRYING HEAT SENSITIVE PRODUCTS Heinz Ravet, Koln, Germany, assignor to National Research Corporation, Cambridge, Mass, a corporation of Massachusetts Filed Nov. 15, 1957, Ser. No. 696,697 Claims priority, application Germany Nov. 17, 1956 3 Claims. (Cl. 34-92) Devices are already known in which the drying of sensitive substances, for example synthetic fiber raw materials and organic fiber materials, is carried out in a super-heated steam atmosphere. The presently disclosed invention stems from the problem of attaining a specially effective and economical construction of such a drying unit. The unit is made in such a way that first a crude drying is carried out in a current of super-heated steam which is supplemented by a more complete drying under high vacuum.

The present invention is directed to an improved apparatus and process wherein a dehydration unit for the crude and fine drying of sensitive substances employs a drying medium, which is circulated in a continuous manner and serves as a heat carrier which acts on the material to be dried. The circulation of the drying medium is by means of a rotary compressor (blower) which is preferably of the Roots type. This is connected in a continuous circulatory system between a condenser and a steam heater.

A preferred form of such a unit employs the rotary compressor first during the so-called crude drying for circulating the chiefly vapor-phase (e.g. steam) drying medium. The rotary compressor is then connected, after the shift to fine drying, as the high vacuum stage of a multistage pump set-up.

The unit can be further developed in a favorable way so that a heated drying vessel is provided for receiving the material to be dried, this vessel being connected to the rotary compressor through a continuous circuit with a condenser. A super-heater for steam is preferably located in the continuous system between the rotary compressor and drying vessel.

A multistage gas ballast pump is preferably provided for the pre-evacuating of the continuous system and as the fore pump for the high vacuum pump in the fine drying of the material. This pump can be connected to the continuous system between the rotary compressor and the steam superheater.

A unit so constructed in contrast to arrangements with isolated steam generators, perhaps steam boilers, has important advantages. The necessary steam comes from the very material to be dried. For this it is necessary that the material at the start have a satisfactory amount of moisture. This condition, however, always exists when using dehydration in a current of super-heated steam, since this process is mainly considered for crude drying.

In the drawing there is a diagram of an example of the invention. Of course, other arrangements can be ad vantageously made by application of the idea in the invention.

In a drying chamber 1, which is provided with a heater 2 preferably in the form of a super-heated steam coil, there is located the material 4 to be dried on a perforated support 3. From the drying chamber 1 a continuous conduit '5 leads next to a steam condenser 6 which has on the inside corresponding cooling surfaces in the form of a condenser coil 7. At the steam condenser there is attached, in a known manner, a trap 14.

The continuous conduit leads further to a Roots type rotary compressor 8 and from there into a steam superheater 9 where a heating medium in a heating coil 10 can be introduced. From the steam heater 9 the continuous conduit 5 can finally be brought again to the drying chamber 1 from which it started. Thus, there exists a closed circuit for the gaseous drying medium. Between the rotary compressor 8 and the steam superheater 9, there is inserted into the continuous conduit 5 a further supply line '11 which, by means of valve 12, is connected with a pump for removal of the vapor-containing mix ture, preferably a gas ballast pump 13 which is preferably two-stage. Between the Roots compressor 8 and the steam superheater there is a valve 15 in the continuous conduit 5.

The operation of the unit is as follows: First the material to be dried 4 is placed on the perforated support 3 and introduced into the drying chamber 1. The heating device 2 on the drying chamber 1 as well as the condenser coils 7 in the condenser 6 and the heating coils 10 in the steam superheater 9 are still not yet in operation. The rotary compressor 8 likewise is not operating. The valves 15 and 12 are opened, the gas ballast pump 13 is placed in operation and there is a pre-evacuation of the entire system (i.e., drying chamber 1, continuous conduit 5, condenser 6, rotary compressor 8, and steam superheater 9). example a few mm. Hg Abs. are obtained, the valve 12 is closed and the two-stage gas ballast pump 13 stopped. Now the material to be dried, which lies on the perforated support 3, is heated by bringing steam to the heater 2 so that an adequate amount of steam is formed. At the same time, the condenser 6 and the steam superheater 9 are put into operation, while through the cooling coils 7 of the condenser 6 is circulated a coolant of appropriate temperature, preferably cold water. Likewise, a suitable heating medium is circulating through the heating coil 10 of the steam superheater. Now, too, the rotary compressor 8 is switched on and there begins a circulation of the gaseous drying medium which originates in the charging material. The saturated steam leaves the drying chamber 1 and is deposited in part on the condenser 6. The steam leaving condenser 6 now travels through the continuous circuit into the rotary compressor 8, which causes the circulation to occur. From there the steam is circulated into the steam superheater 9 and is superheated by the heating coil 10. The super-heated steam enters anew into the drying chamber and can again remove moisture from the material being dried. The circulating process described is continued until the desired crude drying is finished.

At this point the crude drying is interrupted and the unit now switched to fine drying. This is accomplished by shutting off trap '14 and closing valve 15, While at the same time opening valve 12. The rotary compressor 8, which has been up to this point causing the circulation of the current of steam, now serves as the high vacuum pump to which is connected the two-stage gas ballast pump 13 through feed line 11. Thereby there occurs evacuation of the inner chamber of the drying area 1 to lower pressures so that the existing steam is now removed from the system. Thus, under further pumping with increasing vacuum a fine drying occurs. To this end an additional heating of the material being dried can be accomplished for which it is possible to utilize in the fine drying the heat generated during the crude drying so that further heating need not be used.

Especially advantageous is the use in the present arrangement of the rotary compressor which during the crude drying process causes the circulation of the steam current and after the switch to fine drying serves as high vacuum pump. When the gas ballast pump inserted is two-stage very low final pressures in the micron range After correspondingly lower pressure values, for- (of the order of magnitude of 10- mm. Hg Abs.) can be attained.

The heating of the drying chamber 1 in the crude drying process and the cooling action of the condenser 6 must be so related to each other in the operation of the unit during the crude drying that the desired steam partial pressure (e.g. 1 mm. Hg Abs.) exists in the system. During the subsequent .fine drying the condenser 6 and steam superheater 9 can be disconnected by interruption of the corresponding operating mechanism for the cooling coils 7 and for the heating coils 10.

Since certain changes may be made in the above apparatus without departing from the scope of the invention herein involved, it is intended that all matter contained in the above description, and shown in the accompanying drawing, shall be interpreted as illustrative and not in a limiting sense.

What is claimed is:

1. A vacuum drying apparatus for drying heat-sensitive products, said drying apparatus being of the type wherein continuously recirculating steam at subatrnospheric pressure is employed for heating the product to be dried, said apparatus comprising means defining a drying chamber for holding the product to be dried, a condenser, a blower for circulating steam, a steam superheater, a first conduit means for connecting the drying chamber, the condenser, the blower and the superheater in series so that the blower can circulate superheated steam across the product to be dried, through the condenser, through the blower and back through the superheater, a first valve means in said first conduit means between the blower and drying chamber on the exit side of the blower, a second conduit means connected to the first conduit means between the blower and the first valve means, a backing vacuum pump connected to said second conduit means and a second valve means for isolating said backing pump from said first conduit means, whereby said first and second valves when open permit pie-evacuation of said drying apparatus by the backing vacuum pump and permit connection of said blower and backing vacuum pump in series to provide a pressure on the order of 10 mm. Hg Abs. at the inlet of the blower and a correspondingly low pressure over the product to be dried when said first valve is closed and said second valve is open.

2. The drying unit of claim 1 wherein the compressor is a positive displacement blower of the Roots type.

3. The drying unit of claim 1 wherein the backing vacuum pump is a gas ballast pump.

References Citedin the file of this patent UNITED STATES PATENTS Re. 24,260 Thies Dec. 25, 1956 1,324,072 Shorman Dec. 9, 1919 1,799,248 Reinhardt Apr. 7, 1931 2,080,179 Merriam et a1 May 11, 1937 2,285,331 Doyle June 2, 1942

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1324072 *Jun 4, 1913Dec 9, 1919 Pbocess of and apparatus fob dehydbating fruits
US1799248 *Nov 10, 1924Apr 7, 1931Willard Storage Battery CoMethod of drying articles
US2080179 *Jul 10, 1936May 11, 1937Guardite CorpTreatment of organic products
US2285331 *Oct 17, 1939Jun 2, 1942Ingersoll Rand CoApparatus for treating organic material
USRE24260 *Mar 18, 1952Dec 25, 1956Firma BProcess for drying textiles
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3238638 *Mar 8, 1962Mar 8, 1966Pennsalt Chemicals CorpFlow through type drying apparatus
US3239942 *Apr 16, 1962Mar 15, 1966Battelle Development CorpProcess for drying food
US3263335 *Oct 31, 1963Aug 2, 1966United Fruit CoProcess and apparatus for freeze drying utilizing dry gas
US4204379 *Sep 5, 1978May 27, 1980W. R. Grace & Co.Closed circuit shrink tunnel
US4209914 *Dec 9, 1977Jul 1, 1980Projectus Industriprodukter AktiebolagMethod and device for drying machine parts
US4590683 *Oct 5, 1984May 27, 1986Mtm Obermaier Gmbh & Co. KgMethod of and apparatus for drying wound fiber or yarn
US5678759 *Jul 19, 1993Oct 21, 1997Grenci; Charles AlbertHeat generation through mechanical molecular gas agitation
US6922912 *Apr 25, 2002Aug 2, 2005Dyson LimitedDrying apparatus
USRE28965 *Feb 29, 1968Sep 21, 1976Pennwalt CorporationFlow through type drying apparatus
EP0026716A1 *Oct 1, 1980Apr 8, 1981Centre Technique Industriel dit INSTITUT TEXTILE DE FRANCEMethod and apparatus for decreasing the liquid content of a porous material by means of superheated vapour of that liquid
EP0435305A2 *Dec 28, 1990Jul 3, 1991MASCHINEN WITTE GmbH & CO. KGDevice for the drying of sewage sludges
EP0708715A1 *Jul 14, 1994May 1, 1996CLAYTON, R., DallasHeat generation through mechanical molecular agitation
U.S. Classification34/92, 34/403
International ClassificationF26B5/04, F26B21/06, F26B21/08
Cooperative ClassificationF26B21/086, F26B5/04
European ClassificationF26B5/04, F26B21/08C