US3675336A - Method for drying wood - Google Patents

Method for drying wood Download PDF

Info

Publication number
US3675336A
US3675336A US847511A US3675336DA US3675336A US 3675336 A US3675336 A US 3675336A US 847511 A US847511 A US 847511A US 3675336D A US3675336D A US 3675336DA US 3675336 A US3675336 A US 3675336A
Authority
US
United States
Prior art keywords
wood
drying
less
treated
water
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
Application number
US847511A
Inventor
Dallas S Dedrick
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Weyerhaeuser Co
Original Assignee
Weyerhaeuser Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Weyerhaeuser Co filed Critical Weyerhaeuser Co
Application granted granted Critical
Publication of US3675336A publication Critical patent/US3675336A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2210/00Drying processes and machines for solid objects characterised by the specific requirements of the drying good
    • F26B2210/16Wood, e.g. lumber, timber

Definitions

  • the process as herein described is relatively inexpensive and can be used in conjunction with conventional kiln-drying techniques.
  • wood can be dried at faster rates with less degrade, fewer stresses, smaller shell-to core moisture gradients, less shrinkage, fewer wet pockets, and less energy per unit mass of moisture removed.
  • This invention relates to an improvement in the drying of wood comprising treating the wood to be dried with a material capable of reducing the interfacial tension of the water-air boundaries within the cell structure of the wood prior to subjecting the wood to drying by conventional or other convective heating methods.
  • the material used to treat the wood is a surface-active agent or agents in aqueous solution giving a water-air interfacial tension of 30 ergs/cm, or less.
  • the process of this invention can be most easily carried out by spraying, dipping, brushing, etc., an aqueous solution of a surface-active agent on the surfaces of the wood to be dried.
  • a surface-active agent on the surfaces of the wood to be dried.
  • the surfactant does not penetrate very deeply into the wood. This is probably because wood does not have a continuous water phase which is necessary for migration of the surfactant.
  • the wood can be treated, if desired, so that the surfactant or surfactants will be substantially completely diffused throughout the wood although this is not ordinarily necessary.
  • the aqueous solution containing the surfactant when used to treat wood surfaces, penetrates a short distance into the wood surfaces and fills parts of the lumens and particularly the pits connecting lumens with adjacent lumens, and lumens with transverse ray cells with the low surface tension liquid.
  • the pit openings and cell passages in the wood are pulled shut by forces generally present during drying of the wood, with water evaporating from the surfaces of the wood when surfactants are not present. Surface stresses are reduced during the early stages of drying by the action of surfactants and, because more of the cell passages are open, drying proceeds at a faster rate with reduced structural degrade.
  • the particular surface-active material or composition used to treat the wood prior to drying does not appear to be critical as long as it is capable of reducing the interfacial tension of the water-air boundaries within the wood treated.
  • aqueous solutions of non-volatile surfactants giving in aqueous solution a water-air interfacial tension of 30 ergs/cm or less are used.
  • the most common surface-active materials which can be used include sodium alkylarylsulfonates, sold under the trade names ALCONOX by Alconox, lnc.; ALKANOLS by E. l.
  • concentration of surfactant in the aqueous solution used to treat the wood surfaces is not critical. A concentration ranging upward from about 0.01 weight percent surfactant can be used.
  • the wood after treatment with the surfactant, can be dried by conventional kiln-drying techniques. Best results are obtained if the wood is subjected to treatment with the surfaceactive agent or agents as soon as possible after exposure of a freshly cut surface. By doing so, reduction of stress and degrade which take place during yard storage, and/or yard drying, is accomplished.
  • Wood species such as redwood, Douglas fir, Western red cedar, Southern pine, hemlock, etc., can all be dried by techniques herein described.
  • wood in the form of lumber, veneer, boards, etc. can be dried by these techniques.
  • EXAMPLE I A series of 2" X l0" Douglas fir boards were dipped in a 0.04 weight percent solid solution of a linear alkyl aryl sulfonate surface-active agent sold under the trade name "MEL- O by Klix Chemical Company. The boards were left in the solution for only 5-l0 seconds. The boards were then removed and stacked in a conventional stickered configuration together with an identical number of control boards which had been dipped in water only. The control and surface treated boards were laid side by side in the kiln in order to make drying conditions as much alike as possible. The load was 8 ft. wide and separated by A inch stickers. The treated and control boards were placed side by side.
  • the boards were then subjected to drying using an entering air temperature adjusted to give a greater than 25 F. drop across the load.
  • the entering air at a velocity of about 300 fpm, had a wet bulb depression of 30 F. ranging up to F. Drying time was 36 hours.
  • Table l the values represent average figures for the 96 boards dried under the previously mentioned conditions.
  • Utilization of the process of the instant invention provides potentially large economic advantages. Material cost is low and treating cost is lowv
  • the invention results in a shorter process time, greater moisture uniformity, less redrying, and particularly, less degrade.
  • a process of drying wood at a faster rate with less degrade, fewer stresses and less total shrinkage by in situ vaporization of water and migration of the vapor outwardly through the surface regions of the wood comprising:

Landscapes

  • 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)
  • Chemical And Physical Treatments For Wood And The Like (AREA)
  • Drying Of Solid Materials (AREA)

Abstract

An improvement in the drying of wood which allows drying at an equal or faster than conventional rate with less degrade, fewer stresses, and less total shrinkage, comprising treating the wood prior to drying with a material capable of reducing the interfacial tension at the water-air boundaries in the cell structure of the wood. Preferably the wood is treated with an aqueous solution of a non-volatile surface active agent, such as an alkylarylsulfonate.

Description

U Umted States Patent 1151 3,675,336 Dedrick 1451 July 11, 1972 54] METHOD FOR DRYING WOOD 2,838,564 6/1958 Norwood ..260/$05 A 987,888 3/l9ll Koenman ..34/9.5 [72] mnsmw' wash 2,500,954 3/1950 Loughborough 34/95 [73] Asignee: Weyerlneuser Company, Tacoma, Wash.
. Primar Eraminer-Frederick L. Matteson [22] Fned' July 1969 Asrismnl Examiner-Hany B, Ramey [2|] Appl. No.: 847,511 AnorneyLeslie G. Noller, John M. Crawford and Kenneth W. Vernon Related US. Application Data [63] Continuation of Ser. No. 690,055, Dec. 13, I967. 1 ABSTRACT An improvement in the drying of wood which allows drying at [52] U.S.Ill an equal or faster man conventional mm ass degrade 2; 5 l3 4 8 fewer stresses, and less total shrinkage, comprising treating l the wood prior to drying with a material capable of reducing I the interfacial tension at the water-air boundaries in the cell [56] Re Cited structure of the wood. Preferably the wood is treated with an UNfl-ED STATES PATENTS aqueous solution of a non-volatile surface active agent, such as an alkylarylsulfonate. 2,l06,468 l/l938 SChrOlh.......,......................34/9.5 UX 2,706,342 4/l955 Willis ..34/9.5 lClalm, NoDrawlngs METHOD FOR DRYING WOOD This application is a continuation of application, Ser. No. 690,055, filed Dec. 13,1967.
BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to an improved process of drying wood wherein the wood is treated prior to drying.
2. Prior Art Relating to the Invention Reducing the moisture content of wood, and particularly wood having moisture contents of or near that of freshly felled wood, in a relatively fast, economical manner, without substantially affecting the properties thereof, has been dealt with extensively. Elaborate drying schemes have been proposed for drying varying species of wood without damaging shrinkage, surface checking, warping, or cupping. Many woods, such as redwood, Wester red cedar, and Hemlock, when dried by conventional kilndrying schemes, develop excessive and irregular shrinkage known as "collapse" or end up with a highly nonuniform moisture content known as wet pockets." Many experts feel that as the free water leaves the cell faces of the wood cells, it exerts a tensile stress of cohesion equal to many atmospheres. These stresses are often great enough to draw the cell wall together, the net effect of which is to collapse the cell or cells, causing a "washboard or corrugated effect on the surfaces of the wood being dried. In less severe situations, when the effect is limited to elements of the cell wall or the pits, the permeability of the structure to movement of vapor may be seriously reduced.
Several ways of avoiding this problem have been propounded, such as substitution of the water contained in the wood cells with a low surface tension organic liquid. These techniques have been designated usually as solvent seasoning. Other chemical means have also been explored as, for example, that disclosed in US. Pat. No. 2,500,954, wherein the surfaces of the wood to be dried are impregnated with a material that generates a gas within the cellular structure of the wood at the temperature of the drying operation. These methods, however, require a large quantity of chemicals, specialized equipment and often present a very high fire hazard.
The process as herein described is relatively inexpensive and can be used in conjunction with conventional kiln-drying techniques. By the process described, wood can be dried at faster rates with less degrade, fewer stresses, smaller shell-to core moisture gradients, less shrinkage, fewer wet pockets, and less energy per unit mass of moisture removed.
SUMMARY OF THE INVENTION This invention relates to an improvement in the drying of wood comprising treating the wood to be dried with a material capable of reducing the interfacial tension of the water-air boundaries within the cell structure of the wood prior to subjecting the wood to drying by conventional or other convective heating methods. Preferably the material used to treat the wood is a surface-active agent or agents in aqueous solution giving a water-air interfacial tension of 30 ergs/cm, or less.
DETAILED DESCRIPTION OF THE INVENTION The process of this invention can be most easily carried out by spraying, dipping, brushing, etc., an aqueous solution of a surface-active agent on the surfaces of the wood to be dried. When only the surfaces of the wood are treated, the surfactant does not penetrate very deeply into the wood. This is probably because wood does not have a continuous water phase which is necessary for migration of the surfactant. By suitable known techniques, however, the wood can be treated, if desired, so that the surfactant or surfactants will be substantially completely diffused throughout the wood although this is not ordinarily necessary. It is thought that the aqueous solution containing the surfactant, when used to treat wood surfaces, penetrates a short distance into the wood surfaces and fills parts of the lumens and particularly the pits connecting lumens with adjacent lumens, and lumens with transverse ray cells with the low surface tension liquid. The pit openings and cell passages in the wood are pulled shut by forces generally present during drying of the wood, with water evaporating from the surfaces of the wood when surfactants are not present. Surface stresses are reduced during the early stages of drying by the action of surfactants and, because more of the cell passages are open, drying proceeds at a faster rate with reduced structural degrade.
The particular surface-active material or composition used to treat the wood prior to drying does not appear to be critical as long as it is capable of reducing the interfacial tension of the water-air boundaries within the wood treated. Preferably, aqueous solutions of non-volatile surfactants giving in aqueous solution a water-air interfacial tension of 30 ergs/cm or less are used. The most common surface-active materials which can be used include sodium alkylarylsulfonates, sold under the trade names ALCONOX by Alconox, lnc.; ALKANOLS by E. l. duPont de Nemours and Co., Inc.; ARTIC SYNTEX I-ID by Colgate-Palmolive Co., alcohol such as sodium lauryl sulfate; alkyl sulfonates wherein the alkyl group contains from l2 to 18 carbon atoms; alkyl phenol polyglycol ether carboxylic acids having the formula wherein n is [0 to 20 and x is an integer ranging from 1 to 5; and other known surface-active agents. The concentration of surfactant in the aqueous solution used to treat the wood surfaces is not critical. A concentration ranging upward from about 0.01 weight percent surfactant can be used.
The wood, after treatment with the surfactant, can be dried by conventional kiln-drying techniques. Best results are obtained if the wood is subjected to treatment with the surfaceactive agent or agents as soon as possible after exposure of a freshly cut surface. By doing so, reduction of stress and degrade which take place during yard storage, and/or yard drying, is accomplished.
Various species, as well as various configurations of wood, can be dried by the process herein described. Wood species such as redwood, Douglas fir, Western red cedar, Southern pine, hemlock, etc., can all be dried by techniques herein described. In addition, wood in the form of lumber, veneer, boards, etc., can be dried by these techniques.
The following examples are given as merely exemplary of the invention, and are not considered to be limiting in any manner.
EXAMPLE I A series of 2" X l0" Douglas fir boards were dipped in a 0.04 weight percent solid solution of a linear alkyl aryl sulfonate surface-active agent sold under the trade name "MEL- O by Klix Chemical Company. The boards were left in the solution for only 5-l0 seconds. The boards were then removed and stacked in a conventional stickered configuration together with an identical number of control boards which had been dipped in water only. The control and surface treated boards were laid side by side in the kiln in order to make drying conditions as much alike as possible. The load was 8 ft. wide and separated by A inch stickers. The treated and control boards were placed side by side.
The boards were then subjected to drying using an entering air temperature adjusted to give a greater than 25 F. drop across the load. The entering air, at a velocity of about 300 fpm, had a wet bulb depression of 30 F. ranging up to F. Drying time was 36 hours.
In Table l the values represent average figures for the 96 boards dried under the previously mentioned conditions.
TABLEI 2" X l" Douglas Fir Kiln Green dry Shell mois mois mois- Core lure Oven Kiln ture ture mois- Green oondry dry conconlure wt. tent wt. wt. tent tent content Controlboards 39.578 43.90 27.585 30.479 I045 6.65 14.25 Surfactant treatedhoards 40.06] 43.32
EXAMPLE ll Further experiments were carried out under the same conditions as described in Example I, using, however, 2" X hemlock and a drying time of 48 hours. The results are reported in Table ll.
By reference to these two examples, it will be noted that (I moisture content of the treated boards averaged lower than the untreated boards, (2) core moisture contents of the treated boards are lower than for the control boards indicating less tendency toward formation ofwet pockets," (3 shell-tocore moisture content gradients averaged less for treated than control specimens, indicating less shell-to-core stress, and (4) severity of degrade was statistically less for the treated than for the control specimens.
Utilization of the process of the instant invention provides potentially large economic advantages. Material cost is low and treating cost is lowv The invention results in a shorter process time, greater moisture uniformity, less redrying, and particularly, less degrade.
The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:
I. A process of drying wood at a faster rate with less degrade, fewer stresses and less total shrinkage by in situ vaporization of water and migration of the vapor outwardly through the surface regions of the wood comprising:
a. applying to the wood, prior to drying, a material capable of reducing the interfacial tension at the water-air boundaries within the cell structure of the wood, and
b. drying said wood in the presence of said material within an appropriate drying apparatus, and wherein said sur' face-active agent comprises an alkylarylsulfonate.
US847511A 1969-07-17 1969-07-17 Method for drying wood Expired - Lifetime US3675336A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US84751169A 1969-07-17 1969-07-17

Publications (1)

Publication Number Publication Date
US3675336A true US3675336A (en) 1972-07-11

Family

ID=25300810

Family Applications (1)

Application Number Title Priority Date Filing Date
US847511A Expired - Lifetime US3675336A (en) 1969-07-17 1969-07-17 Method for drying wood

Country Status (1)

Country Link
US (1) US3675336A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4229507A (en) * 1978-02-17 1980-10-21 Asahi-Dow Limited Method for drying wood material
EP0143095A2 (en) * 1983-11-16 1985-05-29 Televerket Method for producing in wood a case for a telephone apparatus, a hand microtelephone or some other casing used within the telecommunications industry
WO2004056541A1 (en) * 2002-12-23 2004-07-08 Rajkova Aleksandra Aleksandrov Preparation method for drying timber
US20110131829A1 (en) * 2009-06-05 2011-06-09 Megtec Systems, Inc. Infrared Float Bar
AU2011101450B4 (en) * 2009-06-05 2013-09-05 Babcock & Wilcox Megtec, Llc Improved infrared float bar

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US987888A (en) * 1910-05-31 1911-03-28 Konstantin Koenman Process of treating wood.
US2106468A (en) * 1936-11-23 1938-01-25 Ernest H Schroth Method of making wood products
US2500954A (en) * 1947-03-04 1950-03-21 Us Agriculture Method involving the use of chemicals for increasing the drying rate of wood
US2706342A (en) * 1949-11-04 1955-04-19 Oscar C Sundsby Veneer drying methods
US2838564A (en) * 1956-04-25 1958-06-10 Tennessee Corp Production of surface active materials

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US987888A (en) * 1910-05-31 1911-03-28 Konstantin Koenman Process of treating wood.
US2106468A (en) * 1936-11-23 1938-01-25 Ernest H Schroth Method of making wood products
US2500954A (en) * 1947-03-04 1950-03-21 Us Agriculture Method involving the use of chemicals for increasing the drying rate of wood
US2706342A (en) * 1949-11-04 1955-04-19 Oscar C Sundsby Veneer drying methods
US2838564A (en) * 1956-04-25 1958-06-10 Tennessee Corp Production of surface active materials

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4229507A (en) * 1978-02-17 1980-10-21 Asahi-Dow Limited Method for drying wood material
EP0143095A2 (en) * 1983-11-16 1985-05-29 Televerket Method for producing in wood a case for a telephone apparatus, a hand microtelephone or some other casing used within the telecommunications industry
EP0143095A3 (en) * 1983-11-16 1987-06-03 Televerket Method for producing in wood a case for a telephone apparatus, a hand microtelephone or some other casing used within the telecommunications industry
US4781778A (en) * 1983-11-16 1988-11-01 Stig Olofsson Method for manufacturing in wood cases used within the telecommunications industry
WO2004056541A1 (en) * 2002-12-23 2004-07-08 Rajkova Aleksandra Aleksandrov Preparation method for drying timber
US20110131829A1 (en) * 2009-06-05 2011-06-09 Megtec Systems, Inc. Infrared Float Bar
US20130104414A1 (en) * 2009-06-05 2013-05-02 Megtec Systems, Inc. Infrared Float Bar
AU2011101450B4 (en) * 2009-06-05 2013-09-05 Babcock & Wilcox Megtec, Llc Improved infrared float bar
US9228779B2 (en) 2009-06-05 2016-01-05 Megtec Systems, Inc. Infrared float bar
US9746235B2 (en) 2009-06-05 2017-08-29 Megtec Systems, Inc. Infrared float bar
US10139159B2 (en) * 2009-06-05 2018-11-27 Babcock & Wilcox Megtec, Llc Infrared float bar
US10371443B2 (en) 2009-06-05 2019-08-06 Durr Megtec, Llc Infrared float bar

Similar Documents

Publication Publication Date Title
US3986268A (en) Process and apparatus for seasoning wood
Stamm et al. Dimensional stabilization of wood.
JPH02235702A (en) Method for accelerating fluid movement in wood
US3675336A (en) Method for drying wood
US2417995A (en) Acetylation of lignocellulosic board materials
JP3538194B2 (en) Production method of noncombustible wood
US5024861A (en) Gaseous or vapor phase treatment of wood with boron preservatives
FI71259C (en) SAETT ATT TORKA IMPREGNERAT VIRKE OCH ANDRA IMPREGNERADE CELLULOSABASERADE MATERIAL
US2395311A (en) Treatment of wood
JPH0649283B2 (en) Wood material improvement method
US2500954A (en) Method involving the use of chemicals for increasing the drying rate of wood
FI117126B (en) Use of timber treated with fire retardant and biocide in individual zones and on an industrial scale
US2347635A (en) Chemical seasoning of wood
CN108515596B (en) A kind of preparation method of insect prevention timber
US4233753A (en) Method for preventing the splitting of logs during drying
US1732420A (en) Process for treating, impregnating, seasoning, and stabilizing wood
US2572070A (en) Method of stabilizing wood
JPH06213568A (en) Device for improving quality of wood
JPS5952604A (en) Quality improving agent for wood
SU670434A1 (en) Timber treatment method
US1396899A (en) Process of treating wood
US3616544A (en) Method of drying lumber
US2706342A (en) Veneer drying methods
US1991811A (en) Impregnating wood and the like
US2919492A (en) Process for humidifying hardboard