US2507190A - Process for drying lumber - Google Patents

Process for drying lumber Download PDF

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US2507190A
US2507190A US642034A US64203446A US2507190A US 2507190 A US2507190 A US 2507190A US 642034 A US642034 A US 642034A US 64203446 A US64203446 A US 64203446A US 2507190 A US2507190 A US 2507190A
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drying
lumber
tank
temperature
liquid
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US642034A
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Sr Beverly E Barksdale
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B5/00Drying solid materials or objects by processes not involving the application of heat
    • F26B5/005Drying solid materials or objects by processes not involving the application of heat by dipping them into or mixing them with a chemical liquid, e.g. organic; chemical, e.g. organic, dewatering aids

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  • The-object -o'f ivmy 5invention is to provide 'la novel -4process f-forf'diying green lumber more quickly than has been possible heretofore. vItis also myobjectto-attainlthisresult by a process which will not causeiires.
  • I provide a steel tank A which is equipped with heating coils B that will produce suiicient radiation of heat at given temperatures and pressures.
  • a pipe C leads from the boiler to the heating coil B.
  • a temperature control instrument I which is so regulated that a denite control of temperature over a period of time necessary to dry the wood to a given or stated or required moisture content is obtained by setting or regulating this instrument at certain deiinite temperatures.
  • a gage 2 is provided which indicates the steam pressure in the heating coils.
  • a pipe line 3 is provided through which the drying iluid is pumped intov the tank A.
  • An outlet pipe D opens out from the bottom of the tank and has a strainer 4 where fluid is drained from the tank after drying time and is for the purpose of trapping those objects which are foreign to the fluid, as for example, sawdust, shavings, chips, etc.
  • a pressure steam-controlled valve 5 which can be regulated so as to control the pressure on the steam coils B ⁇ and prevent rupture or bursting of same due to excess pressure.
  • the timing apparatus 6 is provided to govern the time of operation involved and is equipped with an element which indicates when the termination of the required drying period has been reached.
  • the tank has hinged door 'I equipped with staybolts 'la that allow the door to be lowered or opened so that trucks may pass in or out of the tank.
  • Doors l may be provided on either end of the tank or on both ends to permit a continuous operation in supplying and removing lumber.
  • Rails 9 are provided on the door and on the body of the tank to permit passage of trucks from the finv'theltank.
  • Theed'oor r ⁇ i ⁇ is equipped with r aisteel tongue Hl which Vseats -in'a' corresponding groove LIta lin theend-Iof thetank containingv a'gasket ftoepreventthe leaking of fluid fr'omthe tank.
  • V.green llumber fto'be dried isV placed on trucks in themannerlshowniiniFig. 2 and the vtruck of lumberfis"-then--rolle'diinto lthe'tank A, either by hand or mechanically. The material is then anchored in the tank in such a manner as to prevent floating.
  • the tank is then lled with a mineral fluid, preferably of a high paraiiin content such as Texas S. A. E. oil, 6 to 8 weight or viscosity.
  • a mineral fluid preferably of a high paraiiin content such as Texas S. A. E. oil, 6 to 8 weight or viscosity.
  • the relative temperature of the drying fluid and the material to be dried must not exceed 20 degrees Fahrenheit. This prevents the drying fluid from entering or penetrating the material to be dried.
  • the material to be dried is to be covered completely, the same being submerged in the drying fluid.
  • steam control valve 5 is opened to permit the flow of steam not in excess of pounds pressure which flows through thermostatic control valve No. 1 into the steam coils until the temperature of the fluid has reached 250 degrees Fahrenheit. Control Valve No.
  • timing apparatus No. 6 is set for a period of time to be determined by the size and nature of the product being dried. Pressure on the coils is constantly checked by gage No. 2.
  • drying fluid is rapidly drained from the tank, the heat being maintained on the steam coils to prevent any change in temperature of the fluid or wood so that uid will notl enter or penetrate the material being dried. It is important to maintain a substantially uniform temperature during the drying period for the drying of different sizes and species of wood, and also to maintain this temperature while the drying iiuid is being drained from the tank.
  • a slight lm of oil may be left on the top of the lumber but this is quickly removed when it is dressed in a planing mill.
  • the drying liquid can be used again and again, as it is not absorbed by the wood, provided my process is followed. In case it is desired to use the drying liquid again shortly after it is removed from the drying tank, then it is run through a cooling tower, which can be attached to said tank.
  • a process for drying lumber comprising stacking lumber in a tank in such an arrangement that substantially the entire area of each piece is exposed, immersing said lumber in a drying liquid of high paramn content, the tempera- :ture diierential between said liquid and said lumber being not greater than 20 F. whereby penetration of the lumber by the liquid is prevented, raising the temperature of the liquid to approximately 250 F'. and upon reaching temperature equilibrium between said lumber and said liquid maintaining this temperature for a sufcient period of time to vaporize and drive off substantially all of the moisture contained on the particular species of lumber being dried, the temperature at which said liquid vaporizes being substantially above 250 F.
  • a process for drying lumber comprising arranging lumber in a tank in such a manner that substantially the entire area of each piece is exposed, immersing said lumber in a drying liquid, the temperature diierential between said liquid and said lumber being not greater than 20 F. whereby penetration of the lumber by the liquid is prevented, raising the temperature of the liquid to approximately 250 F. and upon reaching temperature equilibrium between said REFERENCES CITED

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (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

May 9, 1950 B. E. BARKSDALE, SR
PROCESS FOR DRYING LUMBER Filed Jan. 18, 1946 ./5. E. .BA/MSDALE, S.
y @KM Patented May 9, 4195() .UNI fra-ED 1 #STATE s ,.PArEN-r o1-Fica vrRocEss-Ftm DRYINGIIEUMBER -Beverly E. Barksdale, Sr., Charlotte, N. C. .nppiicatiunranuary 1s, 11946 serial No5-'642,034
(crei-1.9.5)
. j2 Claims. 1
The-object -o'f ivmy 5invention is to provide 'la novel -4process f-forf'diying green lumber more quickly than has been possible heretofore. vItis also myobjectto-attainlthisresult by a process which will not causeiires.
The apparatus ydisclosed Aherein is claimed in lmy prior United States Patenti No. 2,464,429
which issued on March 15, 1949.
In carrying out :myiprocessl prefer to use the apparatus illustrated inthe accompanying draw ings -i`n Y which:
Referring to the accompanying drawings, I provide a steel tank A which is equipped with heating coils B that will produce suiicient radiation of heat at given temperatures and pressures. A pipe C leads from the boiler to the heating coil B. Mounted on the pipe C is a temperature control instrument I which is so regulated that a denite control of temperature over a period of time necessary to dry the wood to a given or stated or required moisture content is obtained by setting or regulating this instrument at certain deiinite temperatures. A gage 2 is provided which indicates the steam pressure in the heating coils. A pipe line 3 is provided through which the drying iluid is pumped intov the tank A. An outlet pipe D opens out from the bottom of the tank and has a strainer 4 where fluid is drained from the tank after drying time and is for the purpose of trapping those objects which are foreign to the fluid, as for example, sawdust, shavings, chips, etc.
Also mounted in the intake steam pipe C is a pressure steam-controlled valve 5 which can be regulated so as to control the pressure on the steam coils B` and prevent rupture or bursting of same due to excess pressure. The timing apparatus 6 is provided to govern the time of operation involved and is equipped with an element which indicates when the termination of the required drying period has been reached.
The tank has hinged door 'I equipped with staybolts 'la that allow the door to be lowered or opened so that trucks may pass in or out of the tank. Doors l may be provided on either end of the tank or on both ends to permit a continuous operation in supplying and removing lumber. Rails 9 are provided on the door and on the body of the tank to permit passage of trucks from the finv'theltank. Theed'oor r`i `is equipped with r aisteel tongue Hl which Vseats -in'a' corresponding groove LIta lin theend-Iof thetank containingv a'gasket ftoepreventthe leaking of fluid fr'omthe tank.
The bottomfl f the -t'ruck von "which the green lumber is `placed isprovidedwith sloping-crossymembers l 2, so'thatthe lumberf'being-dried may beplaced @in a sloping @position which allows the iiuid'to-'rapidly drain-from" the upper? surface toi #the vmaterial ib'eing dried. The material is also spaced, asat l l, xfrom the edgeof the truckto allow a VAcomplete circulation fof `ther drying iiuid "around the-girth of each individual piece'o'fmaterialbeing dried.
'The V.green llumber fto'be dried isV placed on trucks in themannerlshowniiniFig. 2 and the vtruck of lumberfis"-then--rolle'diinto lthe'tank A, either by hand or mechanically. The material is then anchored in the tank in such a manner as to prevent floating.
The tank is then lled with a mineral fluid, preferably of a high paraiiin content such as Texas S. A. E. oil, 6 to 8 weight or viscosity. At the time of introduction of the drying fluid and the wood or other material to be dried, the relative temperature of the drying fluid and the material to be dried must not exceed 20 degrees Fahrenheit. This prevents the drying fluid from entering or penetrating the material to be dried. After introduction of drying fluid into the tank, the material to be dried is to be covered completely, the same being submerged in the drying fluid. Then steam control valve 5 is opened to permit the flow of steam not in excess of pounds pressure which flows through thermostatic control valve No. 1 into the steam coils until the temperature of the fluid has reached 250 degrees Fahrenheit. Control Valve No. 1 maintains the correct temperature. This is necessary to prevent the checking, warping or twisting of the material being dried. At the time the drying solution reaches the required temperature, timing apparatus No. 6 is set for a period of time to be determined by the size and nature of the product being dried. Pressure on the coils is constantly checked by gage No. 2.
The required time for proper processing having elapsed, drying fluid is rapidly drained from the tank, the heat being maintained on the steam coils to prevent any change in temperature of the fluid or wood so that uid will notl enter or penetrate the material being dried. It is important to maintain a substantially uniform temperature during the drying period for the drying of different sizes and species of wood, and also to maintain this temperature while the drying iiuid is being drained from the tank.
A slight lm of oil may be left on the top of the lumber but this is quickly removed when it is dressed in a planing mill.
Material is then ready for removal and manufacturing.
The drying liquid can be used again and again, as it is not absorbed by the wood, provided my process is followed. In case it is desired to use the drying liquid again shortly after it is removed from the drying tank, then it is run through a cooling tower, which can be attached to said tank.
What I claim is:
1. A process for drying lumber comprising stacking lumber in a tank in such an arrangement that substantially the entire area of each piece is exposed, immersing said lumber in a drying liquid of high paramn content, the tempera- :ture diierential between said liquid and said lumber being not greater than 20 F. whereby penetration of the lumber by the liquid is prevented, raising the temperature of the liquid to approximately 250 F'. and upon reaching temperature equilibrium between said lumber and said liquid maintaining this temperature for a sufcient period of time to vaporize and drive off substantially all of the moisture contained on the particular species of lumber being dried, the temperature at which said liquid vaporizes being substantially above 250 F. thereby precluding vaporization of said liquid during the drying process, rapidly draining said liquid from said tank while maintaining said temperature whereby creation of a partial vacuum in said lumber is prevented, thus precluding absorption o1' said liquid and removing said lumber from said tank.
2. A process for drying lumber comprising arranging lumber in a tank in such a manner that substantially the entire area of each piece is exposed, immersing said lumber in a drying liquid, the temperature diierential between said liquid and said lumber being not greater than 20 F. whereby penetration of the lumber by the liquid is prevented, raising the temperature of the liquid to approximately 250 F. and upon reaching temperature equilibrium between said REFERENCES CITED The following references are of record in the iile of this patent:
UNITED STATES PATENTS Number Name Date 102,665 Douglas May 3, 1870 517,700 Kimball Apr. 3, 1894 783,868 Jarratt Feb. 28, 1905 990,246 Fetterman Apr. 25, 1911 1,760,444 Secord May 27, 1930 2,216,775 Helson Oct. 8, 1940
US642034A 1946-01-18 1946-01-18 Process for drying lumber Expired - Lifetime US2507190A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2706342A (en) * 1949-11-04 1955-04-19 Oscar C Sundsby Veneer drying methods
US2892261A (en) * 1955-07-01 1959-06-30 Hamilton M Hutchinson Process for the treatment of lumber
US3199211A (en) * 1962-02-16 1965-08-10 Koppers Co Inc Method of preseasoning green or partially seasoned wood

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US102665A (en) * 1870-05-03 Richard a
US517700A (en) * 1894-04-03 Drying-kiln
US783868A (en) * 1904-11-18 1905-02-28 James S Jarratt Method of drying lumber.
US990246A (en) * 1910-05-18 1911-04-25 John L Fetterman Method of seasoning wood.
US1760444A (en) * 1919-10-30 1930-05-27 Frederick A Secord Method of drying materials
US2216775A (en) * 1934-03-30 1940-10-08 James R Helson Method of seasoning wood

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US102665A (en) * 1870-05-03 Richard a
US517700A (en) * 1894-04-03 Drying-kiln
US783868A (en) * 1904-11-18 1905-02-28 James S Jarratt Method of drying lumber.
US990246A (en) * 1910-05-18 1911-04-25 John L Fetterman Method of seasoning wood.
US1760444A (en) * 1919-10-30 1930-05-27 Frederick A Secord Method of drying materials
US2216775A (en) * 1934-03-30 1940-10-08 James R Helson Method of seasoning wood

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2706342A (en) * 1949-11-04 1955-04-19 Oscar C Sundsby Veneer drying methods
US2892261A (en) * 1955-07-01 1959-06-30 Hamilton M Hutchinson Process for the treatment of lumber
US3199211A (en) * 1962-02-16 1965-08-10 Koppers Co Inc Method of preseasoning green or partially seasoned wood

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