Pressure dryer for steam seasoning lumber

A process and apparatus for accelerated drying of green and partially dried lumber at pressures above atmospheric pressure to rapidly remove selected portions of moisture from the wood without degradation of the wood structure. A kiln for performing the method comprises a generally cylindrical kiln chamber to contain a stack of lumber, a by-pass line from the front to the back of the chamber to heat and distribute steam evenly to the lumber surfaces, a pressure-controlled steam vent to regulate kiln temperature, and temperature control to regulate the rate of drying. Conditions of pressure and temperature in the kiln can be regulated by heat added from an external source to equalize and condition the lumber rapidly in steam.

DISCLOSURE OF THE INVENTION 
This invention relates to the drying and seasoning of lumber. 
Most lumber is dried by conventional kiln whereby the moisture content of 
the boards is carefully reduced to a desired level by use of heat to 
vaporize a portion of the moisture in the lumber to produce the seasoned 
lumber. Kiln dried lumber has traditionally been dried at atmospheric 
pressure at temperatures below 200.degree. F. with relative humidity in 
the kiln carefully controlled to avoid degradation of the wood. 
Conventional kiln drying has two major drawbacks: first, it is slow, 
taking from one week to several months depending on wood species and board 
thickness; and second, it is energy inefficient, requiring two to four 
times the minimum energy necessary to evaporate the water. 
High-temperature kiln drying, whereby lumber is dried at temperatures from 
200.degree. to 350.degree. F. at atmospheric pressure has recently been 
used to reduce drying time to less than one day. In such processes, as the 
lumber dries, the moisture content at the surface of the boards drops 
quickly to the equilibrium moisture content, EMC (that moisture content at 
which wood neither gains nor loses moisture at a given humidity and 
temperature), while the interior remains wet. Such processes create steep 
moisture gradients between the surface of the boards and the interior that 
persist as the wood dries and can cause the wood to degrade or to stress 
internally (caseharden). 
For example in conventional kiln drying conditions are initially set in the 
kiln so that EMC is between 15 and 20 percent. In high temperature drying 
at temperatures above 220.degree. F. dry bulb temperature and 190.degree. 
F. wet bulb temperature, the EMC is at most 4%. 
Prior art methods of high temperature drying are shown in U.S. Pat. No. 
3,521,373--Pagnozzi and U.S. Pat. No. 3,971,139--Rochon. 
Normal procedure after drying many wood species, depending upon the final 
use of the wood, is to have an equalizing period, whereupon the variation 
in moisture content between the surface and interior is reduced, followed 
by a conditioning period, whereupon moisture is added to the surface of 
the wood to relieve internal stresses. These equalizing and conditioning 
steps are normally done at temperatures below 180.degree. F. and can take 
several days to complete. 
Other methods previously utilized in drying lumber include chamber drying, 
whereby lumber is dried in an air tight structure, usually done at 
subatmospheric pressures. One example of the prior art being shown in U.S. 
Pat. No. 4,176,466--Pagnozzi where heat and subatmospheric pressure are 
used. The advantage of this process is the faster removal of moisture from 
wood at lower temperatures, thus reducing drying time compared to 
conventional kiln drying. Energy is also conserved because of negligible 
heat loss from leakage and no energy required to heat vented air as in a 
conventional or high-temperature kiln. However, vacuum drying is slow 
compared to a high-temperature drying and difficulties in maintaining high 
enough circulation rates for adequate removal of the water from the 
surface of the wood remain a major problem. 
Prior art methods and apparatus for drying lumber utilizing steam are shown 
in U.S. Pat. No. 4,058,906--Pagnozzi; U.S. Pat. No. 4,127,946--Bucholz 
where a mixture of steam and air are utilized. 
Other prior art methods are shown in U.S. Pat. No. 3,971,139--Rochon; U.S. 
Pat. No. 4,198,763--Kurihara; U.S. Pat. No. 4,176,466--Pagnozzi and U.S. 
Pat. No. 4,017,980--Kleingnether. 
The present invention recognizes that steam has a greater ability to 
transfer heat and requires less blower horsepower to deliver a given 
amount of air; thus, pure steam is a more efficient gas than air-steam 
mixtures to dry wood. 
Attempts to dry large quantities of lumber at elevated temperatures and 
pressures have so far been unsuccessful. Steep moisture and temperature 
gradients throughout the entire load of lumber due to poor heat 
distribution have caused severe defects in the dried lumber. 
Most lumber dryers circulate an air-water vapor or air-steam mixture to 
carry away the evaporated water from the surface of the wood. 
No prior art method is known where air is first evacuated from the kiln and 
steam generated from moisture in the lumber utilized to accomplish the 
drying by circulating and heating the steam. 
SUMMARY OF THE INVENTION 
The present invention provides a more efficient and effective lumber dryer 
by rapid and even circulation of steam throughout the load of lumber to 
insure even heat distribution and allow drying of lumber in steam at 
pressures above the atmospheric pressure and temperatures above 
212.degree. F. 
Moreover, devices within the scope of the present invention provide a means 
of steam removal from the dryer which also controls the temperature in the 
dryer at higher pressures and to mechanically remove a portion of the 
water from wood and remove that water from the dryer without evaporating 
the water. 
The benefit and advantages of the present invention are achieved by a 
process and apparatus in which air is removed from a kiln adapted to 
receive green or partially dried lumber and heat the kiln above 
atmospheric pressure in the presence of circulating steam, which 
facilitates the rapid removal of moisture from the lumber without 
excessive degration to the wood structure. The drying rate is kept 
substantially uniform through the load of lumber by evenly distributing a 
high flow rate of steam over the surface of the boards by the use of 
spacers between the boards and strategically placed baffling in the kiln. 
Also the temperature in the dryer is controlled in connection with the 
pressure in the drying chamber, and not solely with the heat input as in 
those processes of prior art where the heat input to the dryer controls 
the drying temperature. 
More specifically, the process of the present invention consists of the 
steps of placing the green or partially dried wood in an enclosed chamber 
which thereafter is evacuated to remove the air. Heat is applied to the 
chamber until the pressure resulting from evaporation of moisture from the 
lumber reaches the desired value depending on the drying schedule for the 
type of lumber being dried, (normally between 15 and 50 psi), so that 
operating temperatures run between 215.degree. and 350.degree. F. Steam 
circulation rate is regulated so that flows are from 50 to 500 feet per 
minute, generally higher during the initial stages of drying and lower 
during equalizing and conditioning. Water which accumulates on the bottom 
if the drying chamber from condensation of steam or from free water being 
forced out of the ends of the boards by internal pressure in the wood, is 
periodically ejected from the dryer. 
Additional features and advantages of the invention will become apparent 
from the following description, with reference to the accompanying 
drawings, which are not presented by way of limitation.

DETAILED DESCRIPTION OF INVENTION 
Referring to FIGS. 1 and 2 a horizontal cylindrical pressure vessel 1 is 
shown which is closed at one end by a wall 2 and is adapted at the 
opposite end 1A to received a flanged cover member 3 secured to flange 1B 
of vessel 1. Cover member 3 can be carried by a pivotable boom 4 by means 
of a chain 5 to facilitate removal and replacement of cover 3. 
A carriage 6 is provided within vessel 1 and adapted to side on cooperative 
rails 7 selectively located longitudinally inside vessel 1 as shown. 
Wooden boards 8 are stacked on carriage 6 so that the length of the boards 
are parallel to the longitudinal axis of vessel 1 and spacers 9 are 
provided to separate different levels of the boards so that the entire 
surface of each board is exposed. Cover 10, for example, a metal sheet, 
can be placed on top of the lumber stack and weights 11, for example, of 
concrete or other nonmetal dense material, can be placed to restrain the 
lumber from excessive warpage during drying. A back baffle 30 is provided 
adjacent end 1A between the outer wall and the end of of the lumber stack 
as shown to direct steam flow as described hereinafter. 
Within the scope of the present invention a steam circulation bypass 12 can 
be provided and in the example shown, bypass 12 has an inlet 13 at the 
open end of vessel 1 and an outlet 14 adjacent the closed end of vessel 1. 
A blower 16 which can be driven by a variable speed electric motor 17 is 
provided to circulate steam through bypass 12. Within the scope of the 
present invention a heater can be provided to heat the steam flowing 
through bypass 12. 
In the example shown a heater 18, which is a coil supplied with steam or 
some other heat transfer fluid through a source 18 and return 21 is 
provided. A control valve 22 is provided to control flow of heat transfer 
fluid to coil 18 in response to regulator 15 which includes a sensor 20 to 
sense the temperature of vapor from vessel 1 admitted to bypass 12 so that 
vapor in bypass 12 is heated and the drying occurs at a predetermined 
rate. Steam flow to coil 18 is controlled by regulator 15 in response to 
temperatures in bypass 12 measured by sensor 20. 
Within the scope of the present invention the pressure in vessel 1 can be 
controlled, and in the example shown is controlled by venting steam 
through a control valve 23 of a vent line 24 in response to a selected 
pressure measured by a sensing regulator 26 which controls valve 23. A 
pressure relief valve 27 is located on a vessel 1 in the event the 
pressure goes over a predetermined limit. 
If desired, steam can be added to vessel 1 from a steam line 28 through a 
valve 29 and vacuum can be drawn on vessel 1 through vacuum line 31 and 
valve 32. 
Also within the scope of the present invention water can be periodically 
removed from vessel and in the example shown in removed through drain 26 
(FIG. 2) from the bottom of the vessel 1 where a control valve 33 can be 
provided and regulated by, for example a timer 34. 
To further reduce energy consumption (as shown in FIG. 2) vessel 1 can be 
insulated and in the example shown vessel 1, front and back ends 2 and 3 
and the bypass 12 are lined with a layer of thermal insulating material 37 
so that heat loss from the dryer surface is minimal. 
FIG. 2 also illustrates how the steam is evenly circulated over the boards 
in the dryer so that no "short circuiting" occurs. Briefly as shown by 
arrow A, steam is withdrawn, through inlet 13 from the front of vessel 1 
by blower 6 and is emitted through outlet 14 at the rear of vessel 1 to a 
cavity 25 defined between the back baffle 30, for example a metal sheet 
extending across the diameter of vessel 1 at the rear end so that the ends 
of boards 8 are flush against it, and front baffle 35, located as shown in 
FIG. 1; so the steam is directed across the lumber through openings 38 
formed by the spaces 9 between boards 8. The steam then flows to the front 
of vessel 1 as shown by arrows C and then back to the intake 13 as shown 
by arrows D. 
FIG. 3 is a graphic representation of equalization and conditioning of 
lumber at temperatures above 212.degree. F. in the apparatus of this 
invention. In one method in accordance with the present invention the 
moisture content of the lumber is equalized, after drying, by subjecting 
the material to conditions such that the EMC is 1 to 3 percent below the 
final desired moisture content of the wood. The time for equalization 
depends on thickness and wood species. Following equalization, the lumber 
is conditioned under conditions where the temperature and pressure in the 
dryer correspond to an EMC of 5 to 15 percent above the final moisture 
content to which the lumber is to be dried. 
For example, if lumber is to be dried to 6 percent moisture content, as 
shown in FIG. 3, then following the drying period, conditions in the dryer 
will be changed to 240.degree. F. and 16 psi as shown by point F (5% EMC) 
for several hours to equalize and then as shown by point G the conditions 
are changed to 215.degree. F. and 15 psi (14 percent EMC) for several 
hours to condition the lumber. 
In operation the dryer, vessel 1 is loaded with lumber 8 with spaces 9 
between levels of the lumber. Front baffle 35 is secured in place against 
the edge of the stack, for example, by means of bolts, not shown. Front 
cover 3 is closed. A vacuum of 25 inches of mercury is drawn on vessel 1 
through vacuum line 31. Blower 16 is started to circulate water vapor 
released from the lumber by the decreased pressure and the pressure 
regulator 26, heat regulator 15 and timer 34 for the water bleed valve 33 
are set to predetermined set points and activated. The temperature in 
vessel 1 increases as steam is produced from the water evaporated from the 
wood and is heated in bypass 12 until the pressure reaches the set limit 
at which point steam is released from the vent line. Water is removed 
periodically from the water bleed line during operation. 
After the drying cycle, the conditions of temperature and pressure are 
changed to equalize the wood moisture content where steam is added from an 
external source, if and when needed, through a steam line 28. Following 
the equalizing cycle, the conditions of temperature and pressure are 
adjusted to condition the wood to relieve internal stresses where steam 
can be added to the dryer through the steam line 28 as needed and 
described hereinafter. 
EXAMPLES 
The following examples are given to facilitate a more detailed and better 
understanding of the present invention, and are not intended to limit this 
invention to these examples. 
EXAMPLE I 
One hundred board feet of yellow-poplar (1 inch by 4 to 6 inches by 100 
inches), 90 to 118 percent initial moisture content, were placed in stacks 
in a dryer similar to the one in FIG. 1. The boards were dried under the 
following conditions: 
Drying: 
Temperature--230.degree. to 265.degree. F. 
Pressure--19 psi 
Drying Time--30 hours 
The water was automatically drained from the tank every two hours for 90 
seconds. The final moisture content of the lumber was 5 to 6 percent and 
the quality of the lumber was comparable to conventionally kiln-dried 
lumber. Internal stress evaluation by standard procedures known to those 
knowledgeable in the art showed moderate stress remaining in the wood. 
EXAMPLE 2 
On hundred board feet of air-dried red oak (1 inch by 4 to 6 inches by 100 
inches), 17 to 19 percent initial moisture content, were placed in stacks 
in a dryer similar to the one in FIG. 1. The boards were seasoned under 
the following conditions: 
Drying: 
Temperature--240.degree. to 260.degree. F. 
Pressure--19 psi 
Drying time--18 hours 
Equalizing: 
Temperature--240.degree. F. 
Pressure--16 psi 
Equalizing Time--2 hours 
Conditioning: 
Temperature--215.degree. F. 
Pressure--15 psi 
Conditioning Time--4 hours 
The water was automatically drained from the tank every two hours for 90 
seconds during the drying cycle only. Steam was added to the system in the 
equalizing and conditioning cycles. The final moisture content was 6 to 7 
percent and reached in 24 hours total seasoning time. The quality of the 
lumber was comparable to conventionally dried lumber and standard 
procedures for internal stresses showed stresses were relieved. 
While a particular dryer has been illustrated in the invention, variation 
may readily be made without departing from the spirit of the invention. 
Variations and modifications will become apparent to those skilled in the 
art, and it is desired to cover all such variations and modifications 
which are within the scope of the invention. 
CLAIMS OF THE INVENTION 
Described in this invention is a steam pressure dryer and process for 
drying wood not described in other dryers.