US2040227A - Apparatus for drying and heat treating material - Google Patents
Apparatus for drying and heat treating material Download PDFInfo
- Publication number
- US2040227A US2040227A US23212A US2321235A US2040227A US 2040227 A US2040227 A US 2040227A US 23212 A US23212 A US 23212A US 2321235 A US2321235 A US 2321235A US 2040227 A US2040227 A US 2040227A
- Authority
- US
- United States
- Prior art keywords
- drying
- chamber
- heat treating
- medium
- drying chamber
- 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
- 238000001035 drying Methods 0.000 title description 51
- 238000010438 heat treatment Methods 0.000 description 19
- 230000003134 recirculating effect Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 2
- 238000010981 drying operation Methods 0.000 description 1
- 238000005192 partition 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
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/06—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
Definitions
- This invention relates to an apparatus designed to dry and also heat treat material and it relates particularly to the type of dryingapparatus which includes a drying chamber in which the material to be treated is placed, a heating chamber communicating with opposite sides of the'drying chamber and means for causing a continuous re-circulation of the heated drying and/or heat treating medium through the drying cha ber and heating chamber.
- the vulcanizing process in which in order to secure satisfactory results the drying and the heat treating of the material must be carried out within temperature limits of one or two degrees.
- the material being vulcanized will be deleteriously affected if during the drying and vulcanizing operation it is subjected to a temperature above or below the relatively narrow range of one or two degrees.
- This object is attained by providing means for Y producing in the drying chamber a local re-cir- 45 culation of the drying medium in a direction at right angles to its general direction of travel through the drying chamber as it is re-circulated in the closed circuit formed by the drying chamber and the heating chamber.
- the drying or heat treating medium is forced through the heating chamber whereitis heated to the desired temperature and then is introduced into the drying chamber and is moved therethrough back to the heating 66 chamber and during its travel through the drying chamber the heating medium is given a continuous re-circulating movement in a direction at right angles to its movement through the drying chamber. In this way the temperature at all points of the drying chamber is maintained uniform.
- Fig. 1 is a vertical sectional view through an apparatus-embodying my invention taken on substantially the line i-l, Fig. 2. 5
- Fig. 2 is a section on the line 22, Fig. 1.
- l indicates a suitable housing having within it the drying and heat treating chamber 2 and also having a heating chamber I which contains suitable heating, means herein :0 shown in the form of steam pipes 4.
- the heating chamber 3 communicates with the lower end of the drying chamber 2 through a passageway 5 and with the upper end of the drying chamber through apassageway 6, and there is thus estab- -25 lished a closed circuit through said chambers through which the drying medium may be continuously circulated and re-circulated as shown by the' arrows a in Fig. 1.
- This re-circulation of the drying medium is produced by the fan or 30 blower I which is shown as located in the upper part of the heating chamber 3 and which may be operated in any suitable way as by means of a belt pulley 8.
- the fan 1 operates to draw the gaseous or heat treating medium from the dry- 35 ing chamber 2 through the passage 6 and force the same through the heating chamber and over the heating pipes and thence back to the drying chamber again through the passage 5.
- auxiliary fans situated within the drying chamber 2 on opposite sides thereof and located out of line with each other as shown best in Fig. 2.
- auxiliary fans 9, iii are constructed to produce a current of the drying medium in a direction at right angles to that in which it travels through the chamber 1 from the inlet passage 5 to the outlet passage 6.
- the fan I for instance, establishes a cross-current of the drying medium from one side to the other of the chamber 2 as indicated by the arrows b and the fan l0 produces another cross-current in the opposite direction from one side to the other of the chamber 2' as indicated by the arrows c. Since these fans 9, ID are out oi alinement with each other the result is that the two fans produce a local auxiliary recirculation of the drying medium in the chamber 2 as indicated by the arrows b and c, which auxiliary re-circuthe chamber 2 a temperature in which there is no more than two degrees variation between an parts of the chamber.
- a device for drying material with subsequent heat treatment comprising a casing divided by a vertical partition into a drying chamber and a heating chamber, said chambers communicating with each other at both the top and the bottom, heating means in the heating chamber, means to recirculate the drying medium through said chambers successively, two fans in the drying chamber on opposite sides thereof, one being located adjacent the heating chamber and the other adjacent the side of the drying' chamber opposite the heating chamber, said fans operating to direct currents of drying medium across the drying chamber in opposite directions and out of line with each other and transverse to the general recirculating movement of the drying medium through the drying chamber, thereby to form a local recirculating movement within the drying chamber in a direction at right angles to said general recirculating movement, whereby the heated medium which is delivered to the drying chamber is evenly distributed and a substantially uniform temperature is maintained throughout the drying chamber.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Description
7 F. WERNERSSON 2,040,227
APPARATUS FOR DRYING AND HEAT TREATING MATERIAL Filed May 24,.1935
\nvenfor.
Frederik Wernersson by? ATTyS.
Patented May 12, 1936 PATENT OFFICE APPARATUS FOR DRYING AND HEAT TREATING MATERIAL Frederik Wernersson, Copenhagen, Denmark Application May 24, 1935, Serial No. 23,212
1 Claim.
This invention relates to an apparatus designed to dry and also heat treat material and it relates particularly to the type of dryingapparatus which includes a drying chamber in which the material to be treated is placed, a heating chamber communicating with opposite sides of the'drying chamber and means for causing a continuous re-circulation of the heated drying and/or heat treating medium through the drying cha ber and heating chamber.
In an app ratus of this type the drying medium moves through the drying chamber continuously in the same direction and it has been found that frequently the temperature at different parts of the drying chamber will vary by several degrees. While such variation may be unimportant when drying some materials yet for certain purposes it is frequently desirable to maintain the temperature in all parts of the drying chamber at approximately the same point especially where the material in the drying chamber is being subjected to a heat treatment as well as the drying operation. 1
As an example reference may be had to the vulcanizing process in which in order to secure satisfactory results the drying and the heat treating of the material must be carried out within temperature limits of one or two degrees. In some vulcanizing processes the material being vulcanized will be deleteriously affected if during the drying and vulcanizing operation it is subjected to a temperature above or below the relatively narrow range of one or two degrees.
It is an object of the present invention to provide a drying and/or heat treating apparatus operating-on the re-circulating principle abovementioned which. is so constructed that a tem-- perature will be maintained in all parts of the chamber which is -substantially uniform 4 and in which there is not more than one or two degrees variation between any two points in the chamber.
This object is attained by providing means for Y producing in the drying chamber a local re-cir- 45 culation of the drying medium in a direction at right angles to its general direction of travel through the drying chamber as it is re-circulated in the closed circuit formed by the drying chamber and the heating chamber. With my inven- 50 tion, therefore, the drying or heat treating medium is forced through the heating chamber whereitis heated to the desired temperature and then is introduced into the drying chamber and is moved therethrough back to the heating 66 chamber and during its travel through the drying chamber the heating medium is given a continuous re-circulating movement in a direction at right angles to its movement through the drying chamber. In this way the temperature at all points of the drying chamber is maintained uniform.
In order to give an understanding of the invention I have illustrated in the drawing a selected embodiment thereof which will now be described after which the novel features will be 1 pointed out in theappended claim.
In the drawing: Y
. Fig. 1 is a vertical sectional view through an apparatus-embodying my invention taken on substantially the line i-l, Fig. 2. 5
Fig. 2 is a section on the line 22, Fig. 1.
In the drawing, l indicates a suitable housing having within it the drying and heat treating chamber 2 and also having a heating chamber I which contains suitable heating, means herein :0 shown in the form of steam pipes 4. The heating chamber 3 communicates with the lower end of the drying chamber 2 through a passageway 5 and with the upper end of the drying chamber through apassageway 6, and there is thus estab- -25 lished a closed circuit through said chambers through which the drying medium may be continuously circulated and re-circulated as shown by the' arrows a in Fig. 1. This re-circulation of the drying medium is produced by the fan or 30 blower I which is shown as located in the upper part of the heating chamber 3 and which may be operated in any suitable way as by means of a belt pulley 8. The fan 1 operates to draw the gaseous or heat treating medium from the dry- 35 ing chamber 2 through the passage 6 and force the same through the heating chamber and over the heating pipes and thence back to the drying chamber again through the passage 5.
Where the drying medium is passed through 40 the drying chamber continuously in the same direction it frequently happens that a considerable temperature variation will develop in difierent parts of the drying chamber. To avoid this and to provide means for maintaining a uniform temperature in all parts of the drying chamber I provide auxiliary fans. or blowers 9, IO situated within the drying chamber 2 on opposite sides thereof and located out of line with each other as shown best in Fig. 2. These auxiliary fans 9, iii are constructed to produce a current of the drying medium in a direction at right angles to that in which it travels through the chamber 1 from the inlet passage 5 to the outlet passage 6. The fan I, for instance, establishes a cross-current of the drying medium from one side to the other of the chamber 2 as indicated by the arrows b and the fan l0 produces another cross-current in the opposite direction from one side to the other of the chamber 2' as indicated by the arrows c. Since these fans 9, ID are out oi alinement with each other the result is that the two fans produce a local auxiliary recirculation of the drying medium in the chamber 2 as indicated by the arrows b and c, which auxiliary re-circuthe chamber 2 a temperature in which there is no more than two degrees variation between an parts of the chamber. L
I claim:
A device for drying material with subsequent heat treatment comprising a casing divided by a vertical partition into a drying chamber and a heating chamber, said chambers communicating with each other at both the top and the bottom, heating means in the heating chamber, means to recirculate the drying medium through said chambers successively, two fans in the drying chamber on opposite sides thereof, one being located adjacent the heating chamber and the other adjacent the side of the drying' chamber opposite the heating chamber, said fans operating to direct currents of drying medium across the drying chamber in opposite directions and out of line with each other and transverse to the general recirculating movement of the drying medium through the drying chamber, thereby to form a local recirculating movement within the drying chamber in a direction at right angles to said general recirculating movement, whereby the heated medium which is delivered to the drying chamber is evenly distributed and a substantially uniform temperature is maintained throughout the drying chamber.
FREDERIK WERNERSSON.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US23212A US2040227A (en) | 1935-05-24 | 1935-05-24 | Apparatus for drying and heat treating material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US23212A US2040227A (en) | 1935-05-24 | 1935-05-24 | Apparatus for drying and heat treating material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2040227A true US2040227A (en) | 1936-05-12 |
Family
ID=21813722
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US23212A Expired - Lifetime US2040227A (en) | 1935-05-24 | 1935-05-24 | Apparatus for drying and heat treating material |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2040227A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2808237A (en) * | 1953-02-16 | 1957-10-01 | Kenneth E Fosnes | Wall mounted air circulating heat exchangers |
| US3239949A (en) * | 1962-07-25 | 1966-03-15 | Dale E Miles | Drying cabinet |
| US3327404A (en) * | 1964-12-29 | 1967-06-27 | Mark B Ganier | Drying cabinet |
| US6393723B1 (en) | 2000-08-10 | 2002-05-28 | George R. Culp | Forced convection heat exchangers capable of being used in kilns |
| US20080178616A1 (en) * | 2007-01-25 | 2008-07-31 | Leo A. Daly Company | Temperature controlled storage facilities and methods |
-
1935
- 1935-05-24 US US23212A patent/US2040227A/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2808237A (en) * | 1953-02-16 | 1957-10-01 | Kenneth E Fosnes | Wall mounted air circulating heat exchangers |
| US3239949A (en) * | 1962-07-25 | 1966-03-15 | Dale E Miles | Drying cabinet |
| US3327404A (en) * | 1964-12-29 | 1967-06-27 | Mark B Ganier | Drying cabinet |
| US6393723B1 (en) | 2000-08-10 | 2002-05-28 | George R. Culp | Forced convection heat exchangers capable of being used in kilns |
| US20080178616A1 (en) * | 2007-01-25 | 2008-07-31 | Leo A. Daly Company | Temperature controlled storage facilities and methods |
| US7946124B2 (en) | 2007-01-25 | 2011-05-24 | Leo A. Daly Company | Temperature controlled storage facilities and methods |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2083141A (en) | Apparatus for conditioning sheet material | |
| US1994220A (en) | Metal sheet drying oven | |
| US2040227A (en) | Apparatus for drying and heat treating material | |
| US1567031A (en) | Process for treating hygroscopic materials | |
| US2111148A (en) | Drier | |
| US1463923A (en) | Pabeb-dbztkg machihe | |
| US1393086A (en) | Method of and apparatus for drying, conditioning, and regulating tee moisture content of hygroscopic materials | |
| US1353358A (en) | Drying or cooling apparatus | |
| US952775A (en) | Drier. | |
| US2446822A (en) | Method and apparatus for removing volatiles from articles involving the use of infra-red lamps | |
| US2317890A (en) | Vulcanizer | |
| US1577509A (en) | Apparatus for handling vapors | |
| US1495143A (en) | Process and apparatus for treating textile materials | |
| US1971405A (en) | Conditioning of tobacco and similar materials | |
| DE2109696A1 (en) | Device for carrying out a method for drying, in particular fibers and yarns | |
| US1280642A (en) | Tunnel-drier. | |
| US3274697A (en) | Method for conditioning web- or sheetlike material | |
| US1599797A (en) | Method of and apparatus for uniformly drying or processing materials | |
| USRE20745E (en) | Process of drying leather and simi | |
| US2229085A (en) | Vulcanizing apparatus | |
| US811446A (en) | Veneer-drier. | |
| US3052040A (en) | Industrial oven | |
| US1436142A (en) | Apparatus for drying | |
| GB177307A (en) | Improvements in desiccators | |
| US1204945A (en) | Art of finishing and shaping hosiery. |