US905252A - Pulp-drier. - Google Patents
Pulp-drier. Download PDFInfo
- Publication number
- US905252A US905252A US40681407A US1907406814A US905252A US 905252 A US905252 A US 905252A US 40681407 A US40681407 A US 40681407A US 1907406814 A US1907406814 A US 1907406814A US 905252 A US905252 A US 905252A
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- chamber
- tubes
- pulp
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- steam
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
- F26B5/06—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum the process involving freezing
Definitions
- My invention relates to improvementsin pulp driers, one object of which-is to utllize the waste stack gases for drying the pulp without impeding the speed of travel of such gases.
- a further object attained is the regulation ofthe temperatureaof the pulpas itis being driedzf v 'il f
- Still another object-'attained is the release of steam from thefpulp" as itis being dried.
- Another objectattained is the removal of soot deposits from the' drying tubes.
- My invention also attains other objects and consists of novel features'and combinations of parts, all of which will be more fully described hereinafter and ⁇ particularly point- Y ed out in the claims.V
- Figure 1 is a vertical sectional view longitudinally of the apparatus, parts ,being 'broken away;
- Figs. 2 ⁇ and f3 are views of the opposite endsl of the drying chamber;
- Fig. 4 ⁇ is a ⁇ detailr view of one means for accomplishing the removal of soot or other deposits on the drying' tubes;
- Fig.'5 is a detail view of one of the adjustable vents. s
- I - provide a closed chamber (A) and connect the chamber (A) near its rear end with an ⁇ inlet pipe leadingfrom the stack or other waste gas iiue (not shown) into the chamber through the top thereof, and from the lower rear end of the chamber ⁇ I lead the Waste gases deprived of the greater portion of their heat back to the stack or to any other discharge through an foutlet pipe (2).
- Extending from end to end of the drying chamber are a plurality of series of horizontal tubes, and while I have shown but six tubes inl each horizontal series, it is obvious that a' greater or lesser number might be emhe forward ends'of the upper series of ⁇ tubes (5) project beyond the front wall of the machineand are equipped with hoppers (6) (6) to receive the wet pulp, such pulp ybeingfconveyed from end to end of the tubes by means of screw conveyers (7).
- the horizontall series of tubes intermediate the upper and lower series have their opposite ends projecting through, but not beyond the end ⁇ walls ofthe drying chamber, the ends being provided with dampers or adjustable vents (8) (8) for a purpose hereinafter set forth.
- Each tube incloses a screw, the screws in the upper horizontal series adapted to convey the pulp to the rear of the chamber where the upper tubes communicate through down chutes (9) with the rear ends of the next lower series of tubes, the screws in which convey the material toward the front of the chamber until the down chutes (9) connecting the second ⁇ series of tubes with the next lower series is reached and so on, the material being conveyed forward and backward through the drying chamber until the lowest'series ⁇ of tubes (10) is reached, it'being remembered that the ends of such tubes project beyond one end of the cham- (20). Looking at Fig.
- the gears are positively ac tuated in series of threes, the center shaft of each series having a bevel gear (19) thereon adapted to mesh with a beveled pinion (21) carried by a countershaft (22) driven by a power. shaft (23) in the usual manner, the two countershafts extending vertically and equipped with pinions for each series of gears.
- the end gears of each series of gears r'otate in the same direction, whereas the center gear rotates in a direction opposite thereto.
- the rotation of the screws will, of course, tumble and commingle the material, bringing every portion thereof against the -heated sides of the tube, but not allowing it to remain in contact with the tube sufriciently long to burn.
- thermometers (28) on the steam pipes (25) and in the event that the temperature rises'above a predetermined point I may open the vents or dampers, (8) (8) ,thereby admitting cold air to any one or more series of tubes, the air being drawn into the tubes because of the slight vacuum created by the exhauster (27 cooling the tubes and the material therein.
- Thedrawings disclose a batHeplate (13) interposed between the upper three series of tubes and the lower three series, the baffle 'plate extending forwardly from the rear of the chamber between the inlet and outlet pipes (l) and (2), thus diverting the incoming hot gases and causing them ⁇ to travel toward the front of the chamber to envelop the series of tubes from end to end.
- the baffle 'plate extending forwardly from the rear of the chamber between the inlet and outlet pipes (l) and (2), thus diverting the incoming hot gases and causing them ⁇ to travel toward the front of the chamber to envelop the series of tubes from end to end.
- I may use an auxiliary heating furnace, the heat from which is conveyed into the closed chamber (A) through the induction ⁇ pipe (l) and mingles with the fuel or stack gases, or I ymay employ the auxiliary furnace alone without reference to the liuc gases.
- a drier comprising a chamber, conduits for admitting waste gases to the chamber and for permitting their escape, a tube conveyer closed within the chamber to the entrance of hot gases, and means for removing deposits from the exteriors of the conveyer.
- a drier comprising a chamber, conduits for admitting waste gases to the chamber and for permitting their escape, a tube conveyer closed within the chamber to the entrance of hot gases, hollow perforated rings encircling the conveyer at intervals, and a steam connection communicating with the rings.
- tubes being closed to the entrance of hot gases within the chamber, means for permitting the escape of vapor from each tube and means for admitting air to the respecveyers, means for admitting hot vgases to and removing them from the chamber, steam out.- lets located intermediate the ends of each tube, a steam receiving pipe connecting the steam outlets in each bank of tubes, a steam chamber to which the steam pipes lead, means for creating a partial vacuum in the steam chamber, and means for admitting air to the respective tubes and controlling the amount of air so admitted.
- a drier the combination of. a chamber, stationary tubes arranged in banks and extending across the chamber, the tubes at one end passing through the walls of the chamber, chutes within the chamber connecting adjacent tubes, screw conveyers in the tubes, means for rotating the screw conveyers, means'for admitting hot gases to and removing them fromthe chamber, means for permitting the escape of vapor from passing through ⁇ the wall of the chamber being provided with openings to admit air to the respective tubes and adjustable plates HENRY A. VALLEZ.
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- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Molecular Biology (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Description
H. A. VALLI-JZ.v
PULP DRIRE.
APPLIcATIoN FILED 1320.16, 1907.
Patented Dec'. 1, 190s.
2 SHEETS-SHEET 1.
THE NpRRls PE co.. wAsHmawN. n, l:A
H. A; VALIJBZ.
PULP DRIRE.,
APPLICATION FILED DBO. 16,1907.
Patented Dec. 1,1908.
Z SHEETS-SHEET 2.
nl .l llllFllVlllLlll 1HE nomas Ps1-zus ca., nu'snmarou. n. c.
` lENRY'A. VALLEZ, OF BAY CITY, MICHIGAN.
PULP-DRIER.
yspeciaaalon of Letters Patent.
Patented Dec. 1, 1908.
To all whom 'it may concern:
Be it known that I, vHENRY A. VALLEz, a
citizen of the United States, residing at Bay City, in the county Vof Bay and Stateof 'Michigam have invented certain new and useful Improvements inPulp-Driers'; and I Ido hereby declare the following to be a full,
clear, and exact description ofv they invention, such as will enable others skilled in the art to which it appertains to makean'd use thev same. Y
My invention relates to improvementsin pulp driers, one object of which-is to utllize the waste stack gases for drying the pulp without impeding the speed of travel of such gases.
- `.Another object. is to maintain v:the pulp white and clean during the drying operation.
A further object attained is the regulation ofthe temperatureaof the pulpas itis being driedzf v 'il f Still another object-'attained is the release of steam from thefpulp" as itis being dried.
A still further objectfattainedis va perfect circulation of the'hot waste'gases fromthe stack through the drier.
Another objectattained is the removal of soot deposits from the' drying tubes.
My invention also attains other objects and consists of novel features'and combinations of parts, all of which will be more fully described hereinafter and` particularly point- Y ed out in the claims.V
In the accompanying drawings, Figure 1 is a vertical sectional view longitudinally of the apparatus, parts ,being 'broken away;
Figs. 2` and f3 are views of the opposite endsl of the drying chamber; Fig. 4 `is a` detailr view of one means for accomplishing the removal of soot or other deposits on the drying' tubes; and Fig.'5 is a detail view of one of the adjustable vents. s
Hitherto the plan has been tried .of utilizing flue gases to drybeet or other pulp, but it has been found necessary to maintain the same Vdraft or speed of travel of the flue gasesin the drier* that obtains'in the stack 'and such draft is strong enough to carry Vthe light ulp with it. Furthermore, the contact o the gaseswith the pulp discolorsthe pulp and loads it withimpurities.V To ob- Vviate these and other manifest disadvantages, I -provide a closed chamber (A) and connect the chamber (A) near its rear end with an `inlet pipe leadingfrom the stack or other waste gas iiue (not shown) into the chamber through the top thereof, and from the lower rear end of the chamber `I lead the Waste gases deprived of the greater portion of their heat back to the stack or to any other discharge through an foutlet pipe (2). In order to maintain approximately the same speed of circulation of the gases in the drying chamber as is 1naintained in the stack I locate a blower fan 8 in the inlet pipe (l) and an exhaust fan 4t in the outlet pipe (2) I have shown these fans diagrammatically in the drawings.
Extending from end to end of the drying chamber are a plurality of series of horizontal tubes, and while I have shown but six tubes inl each horizontal series, it is obvious that a' greater or lesser number might be emhe forward ends'of the upper series of `tubes (5) project beyond the front wall of the machineand are equipped with hoppers (6) (6) to receive the wet pulp, such pulp ybeingfconveyed from end to end of the tubes by means of screw conveyers (7). The horizontall series of tubes intermediate the upper and lower series have their opposite ends projecting through, but not beyond the end `walls ofthe drying chamber, the ends being provided with dampers or adjustable vents (8) (8) for a purpose hereinafter set forth.
Each tube incloses a screw, the screws in the upper horizontal series adapted to convey the pulp to the rear of the chamber where the upper tubes communicate through down chutes (9) with the rear ends of the next lower series of tubes, the screws in which convey the material toward the front of the chamber until the down chutes (9) connecting the second `series of tubes with the next lower series is reached and so on, the material being conveyed forward and backward through the drying chamber until the lowest'series `of tubes (10) is reached, it'being remembered that the ends of such tubes project beyond one end of the cham- (20). Looking at Fig. 2, it will be seen that for convenience the gears are positively ac tuated in series of threes, the center shaft of each series having a bevel gear (19) thereon adapted to mesh with a beveled pinion (21) carried by a countershaft (22) driven by a power. shaft (23) in the usual manner, the two countershafts extending vertically and equipped with pinions for each series of gears. The end gears of each series of gears r'otate in the same direction, whereas the center gear rotates in a direction opposite thereto. The rotation of the screws will, of course, tumble and commingle the material, bringing every portion thereof against the -heated sides of the tube, but not allowing it to remain in contact with the tube sufriciently long to burn.
It is obvious that the heat 'will evaporate the particles of liquid in the wet pulp and generate steam, and it is desirable to remove this steam to facilitate the drying operation, to which end I provide steam outlets (24) leading from each tube intermediate its ends and connected to steam-receiving pipes (25) 'extending to a steam chamber (26) equipped with an exhaust fan or other suitable device ('27) adaptedto create a partial vacuum or 'rarefaction in the pipes (25) and tubes to withdraw the steam therefrom.
It is also necessary to watch the pulp to prevent its burning and to provide some means for regulating the temperature in the tubes, to which end I provide the thermometers (28) on the steam pipes (25) and in the event that the temperature rises'above a predetermined point I may open the vents or dampers, (8) (8) ,thereby admitting cold air to any one or more series of tubes, the air being drawn into the tubes because of the slight vacuum created by the exhauster (27 cooling the tubes and the material therein.
In the present instance, I have shown six series of horizontally-placed tubes, but it is vobvious that I might use a smaller or larger number of series, and that they need not be horizontal. Thedrawings disclose a batHeplate (13) interposed between the upper three series of tubes and the lower three series, the baffle 'plate extending forwardly from the rear of the chamber between the inlet and outlet pipes (l) and (2), thus diverting the incoming hot gases and causing them `to travel toward the front of the chamber to envelop the series of tubes from end to end. In view ofthe fact that the tubes within the chamber are closedthe heat is conducted to the material through the material of -the `tubes vand the hot i gases do not come into actual contact with the pulp. Also it will be observed that I lead the hot gases into the chamber 'at the point 'where the pulp is wettest, thus'avoiding the danger Aof burning the pulp,as 'well as allowing the point in their peripheries to ay steam-suppl? pipe (16) extending outside the'chainheraml controlled by a valve or cock (not shown). The perforations, facing both ways, will emit steam in opposite directions to remove the deposit from the tubes.
I may use an auxiliary heating furnace, the heat from which is conveyed into the closed chamber (A) through the induction `pipe (l) and mingles with the fuel or stack gases, or I ymay employ the auxiliary furnace alone without reference to the liuc gases..
It is obvious that the advantages hereinbefore mentioned are attained by this invention, and that changes might be made in the form Vand arrangement of the several parts described without departing from the spirit and scope of my invention.
Having thus fully disclosed my invention, what I claim as new isl. A drier comprising a chamber, conduits for admitting waste gases to the chamber and for permitting their escape, a tube conveyer closed within the chamber to the entrance of hot gases, and means for removing deposits from the exteriors of the conveyer.
2. A drier comprising a chamber, conduits for admitting waste gases to the chamber and for permitting their escape, a tube conveyer closed within the chamber to the entrance of hot gases, hollow perforated rings encircling the conveyer at intervals, and a steam connection communicating with the rings.
3. The combination in a drier comprising a closed chamber, stationary tubes extending across the chamber, the tubes at one end projecting through the wall of the chamber, chutes within the chamber connecting each two adjacent tubes, screw conveyers within the respective tubes, means for rotating the screw conveyers, a waste gas conduit leading to the chamber, means for forcing the waste gases into the chamber, an exhaust conduit leading from the chamber,=means in the exhaust conduit for withdrawing the gases from the chamber, the inlet and exhaust conduits communicating with the chamber at the same end, a balie plate extending between the inlet and exhaust conduits, the
tubes being closed to the entrance of hot gases within the chamber, means for permitting the escape of vapor from each tube and means for admitting air to the respecveyers, means for admitting hot vgases to and removing them from the chamber, steam out.- lets located intermediate the ends of each tube, a steam receiving pipe connecting the steam outlets in each bank of tubes, a steam chamber to which the steam pipes lead, means for creating a partial vacuum in the steam chamber, and means for admitting air to the respective tubes and controlling the amount of air so admitted. p
5. In a drier, the combination of. a chamber, stationary tubes arranged in banks and extending across the chamber, the tubes at one end passing through the walls of the chamber, chutes within the chamber connecting adjacent tubes, screw conveyers in the tubes, means for rotating the screw conveyers, means'for admitting hot gases to and removing them fromthe chamber, means for permitting the escape of vapor from passing through `the wall of the chamber being provided with openings to admit air to the respective tubes and adjustable plates HENRY A. VALLEZ.
Witnesses:
Gno. B'. VVILLCOX,l RALPH S. WARFIELD.
lthe respective tubes, the ends of the tubes
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US40681407A US905252A (en) | 1907-12-16 | 1907-12-16 | Pulp-drier. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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US40681407A US905252A (en) | 1907-12-16 | 1907-12-16 | Pulp-drier. |
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US905252A true US905252A (en) | 1908-12-01 |
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US40681407A Expired - Lifetime US905252A (en) | 1907-12-16 | 1907-12-16 | Pulp-drier. |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3027652A (en) * | 1958-01-20 | 1962-04-03 | George W Wallace | Methods and means for simultaneously cleaning and drying finely divided mineral matter such as coal and the like |
-
1907
- 1907-12-16 US US40681407A patent/US905252A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3027652A (en) * | 1958-01-20 | 1962-04-03 | George W Wallace | Methods and means for simultaneously cleaning and drying finely divided mineral matter such as coal and the like |
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