the present inventors have jointly developed a system for incorporating a copper based preservative system , for example the treatment commercially available as the comptec ™ copper ammonium acetate complex wood treatment , in combination with drying oils functioning as described herein , into the manufacturing process for solid wood , plywood , and wood based composites . and combinations thereof . many copper - based wood preservatives are known , and their use is contemplated here . pertinent agricultural drying oils include linseed , soybean , canola , rapeseed , sunflower , tung and castor oils and any other oils derived from agricultural sources . pertinent fish oils , which are also drying oils , can be extracted from sardines , mackerel , codfish ( including but not limited to cod - liver oil ), tuna , salmon , pilchard , menhaden , and herring , as well as other species . for composite panel products , the oil copper combination can be applied to a wet ( green ) or dry wood or wood furnish but is most optimally applied to green or wet wood furnish at a moisture content ( mc ) above the fiber saturation point ( i . e . above 30 % mc ). the use of a green wood furnish ensures that the penetration of the preservative system into wood flakes is maximized for optimum efficacy . in the case of solid lumber , piles , and already manufactured plywood , the copper combination is preferably applied to dry wood at a moisture content around 15 - 19 %. the use of dry wood ensures penetration deep into the wood to maximize penetration . the addition rate for the copper ammonium acetate complex wood treatment formulation may range from 0 . 5 % m / m ( i . e . “ mass - to - mass ” or weight %) active ingredient to 5 % m / m active ingredient defined on a copper ammonium acetate complex basis . the drying oil addition rate may vary from 0 . 5 % to 50 % by weight ( m / m ). the lower limit of drying oil addition can alternatively be 1 %, 1 . 25 %, 2 %, 2 . 5 %, 3 %, 4 %, or 5 % by wood weight , on the same basis . the upper limit of drying oil addition can alternatively be 50 %, 40 %, 30 %, 25 %, 20 %, 15 %, 14 %, or 13 %, or 12 %, or 11 %, or 10 %, or 8 %, or 6 %, or 5 % by wood weight , on the same basis . the decay and termite resistance performance of the finished panels are proportionally linked to the weight percentage of copper ammonium acetate complex wood treatment incorporated into the furnish . similarly , improvements in water absorption and thickness swell is proportionally related to the level of oil incorporated into the matrix . the comptec ™ wood composite treatment and the oil are believed to be synergistic when used to treat solid wood , wood composites , or plywood . their use in wood based composites can provide mechanical panel properties that are superior to those expected with conventional resin systems alone . the increase in mechanical properties correlates with the quantity of oil and copper ammonium acetate complex wood treatment added to the furnish or plies . given a consistent resin loading , as the level of oil increases per given level of copper ammonium acetate complex wood treatment , the mechanical properties improve significantly . the interaction of the copper based wood treatment and oil is believed to create a secondary resin source which enhances the overall furnish to furnish ( particle / flake : particle / flake ) bonding in wood composites . this improves the overall mechanical properties of the finished panel . this interaction is thought to act similarly to a chemical process known as epoxidation in which oils derived from agricultural products can be converted from liquids into either soft or hard plastic compounds . examples of this would be bags used for blood collection and pvc plastic stabilizer for plastic piping used for plumbing . chemically , epoxidation involves the addition of an oxygen bridge to unsaturated oil molecules via a catalytic reaction pathway . in this invention , copper ions are provided by the copper ammonium acetate complex wood treatment . therefore , it is hypothesized that , in the manufacture of wood based composites and plywood , especially during pressing , the active ingredients of the copper ammonium acetate complex wood treatment epoxidize the oil , creating a secondary binding agent for the wood . using both a copper ammonium acetate complex and a drying oil , it is possible to make composite wood products using no other synthetic binding resins that are currently used by industry . these resins include phenol formaldehyde , isocyanates , and urea formaldehyde resins . the treatment of solid wood with an oil and another copper based wood preservative is also contemplated . copper ammonium acetate complex ( comptec ™) and alkaline copper complex wood treatment solutions are two of many copper based formulations that are suitable for this purpose . the treatment solutions can be emulsified using water as a carrier , the oil can be utilized as the carrier of the biocide treatment , or the oil and biocide can be applied separately , as by first treating the wood with the copper complex , then treating it with the reactive oil , which can be applied , for example , in the form of an aqueous emulsion . the reactive oil can alternatively be formulated as part of a water repellent emulsion system that is subsequently applied to the wood , which can also include a binding resin . the copper complex , reactive oil , water repellant , and binding resin , or any subset of them can also be provided as one formulation . the inventors contemplate that if the wax emulsion and the copper complex are present in the same formulation and would otherwise tend to react prematurely , the wax emulsion will partially shield the oil from the copper in this single step emulsion . the copper and oil then will interact when the wax emulsion breaks within the wood . the wood may be treated by pressure treatment , much like other wood treatments are applied to solid wood . one pressure treatment may be used , or a series of two or more pressure treatments may be used . more than one pressure treatment may be applied if the copper complex and reactive oil are added from separate formulations . the copper complex and reactive oil treatments can be carried out at ambient temperature , for example 21 ° c ., at a lower temperature , or at an elevated temperature . for example , although the treatment temperature is not contemplated to be critical , a suitable temperature range is 0 ° c .- 179 ° c ., alternatively 0 ° c .- 119 ° c ., alternatively 0 ° c .- 100 ° c ., alternatively 0 ° c .- 80 ° c ., alternatively 0 ° c .- 60 ° c ., alternatively 0 ° c .- 50 ° c ., alternatively 0 ° c .- 40 ° c ., alternatively a lower limit of any of the preceding ranges of 15 ° c . the epoxidization process is contemplated to improve the mechanical properties of solid wood , as well as preserving it . it is hypothesized that the epoxidation process between the copper ions and reactive oil occurs , or is at least initiated , when the oil / copper treated solid wood is dried using conventional drying equipment to a moisture content appropriate for its eventual end use . an oil / copper treated wood furnish can also be dried using conventional drying equipment to a moisture content appropriate to the type of resin system that is utilized for the specific composite product being manufactured . on the other hand , copper treated wood flakes can be first dried and then sprayed with the oil at the same time as resin and wax are applied in a conventional blender prior to forming and pressing . the moisture content of the furnish treated in this manner can range from 0 . 5 % to 25 % mc based on oven - dry weight of furnish . the dried furnish optionally may be blended with any of a vast variety of resins currently used by the composite wood industry . such resins could include , but are not limited to liquid phenol formaldehyde ( lpf ), powder phenol formaldehyde ( ppf ), acid catalyzed pf resins ( commonly known as novolac resins ), isocyanate ( mdi ), phenol - melamine - formaldehyde adhesives ( pmf ), urea formaldehyde , or combinations of those resins . addition rates may vary from 0 % to 25 % resin solids depending on panel type and application . the dry treated wood furnish is sprayed with resin and wax ( and in some cases the drying oil ), formed and oriented into a mat of the desired thickness and pressed to form the final panel . mats are formed to suit the type of composite and desired end use . formed mats are pressed under heat and pressure conditions appropriate to the final end use of the finished board . typical press parameters include consolidation pressures ranging from 50 psi ( 35 n / cm 2 ) to 650 psi ( 453 n / cm 2 ), cook pressures from 0 psi ( 0 n / cm 2 ) to 400 psi ( 280 n / cm 2 ), and a de - gas segment . typical press temperatures vary from 200 ° f . ( 93 ° c .) to 550 ° f . ( 288 ° c . ), depending on type of composite . press time may vary from 1 minute to 20 minutes duration . resin is applied to the treated plies , which are then formed with specific cross orientation of the veneers , or in the case of laminated veneer lumber all oriented in one direction . the formed billet is transferred into a press and consolidated into the final plywood or structural lumber substitute . typical parameters include consolidation pressures ranging between 50 and 300 psi ( between 35 and 198 n / cm 2 ). typical press temperatures may vary from 200 ° f . ( 93 ° c .) to 550 ° f . ( 288 ° c .). in some cases radio frequency curing may be utilized . the physical and structural characteristics of the oil / copper ammonium acetate complex wood treatment treated composite or plywood panels are equivalent or superior in magnitude to similarly manufactured but untreated or copper ammonium acetate treated composites and plywood that are not treated with an oil . examples illustrating application of the invention using oriented strandboard and medium density fiberboard as the matrix are presented below . five sets of three wood composite panels measuring 21 inches × 21 inches × 12 inch ( 53 cm × 53 cm × 1 . 2 cm ) were manufactured on a laboratory press . one set of panels contained no oil or preservative and served as reference control panels . another set of panels used copper ammonium acetate ( copper ammonium acetate complex wood preservative ) treated flakes without linseed oil and was designed to serve as a reference control . the remaining panels used copper ammonium acetate treated flakes with varying loadings of linseed oil , archer daniels midland &# 39 ; s gp - 1125 . these levels were 1 . 25 %, 2 . 5 %, and 5 . 0 % m / m based on oven dry wood weight . green flakes ( 50 % mc —“ moisture content ”) were treated with copper ammonium acetate alone or in combination with the various levels of oil in a rotary batch type blender equipped with a coil spinning disc atomizer . the flakes were treated with concentrated copper ammonium acetate solution ( 31 . 32 % nominal active ingredient level ) such that the final chemical loading on the flakes was equivalent to 3 . 1 % m / m on an oven dry weight of flakes basis . the treated flakes received a short dwell time ( 30 - 60 seconds ) before drying . the target moisture content after drying was 5 %. one set of flakes was sprayed with liquid phenolic resin at an addition rate of 3 . 5 % solids on an oven dry weight of flakes basis , and a second batch was blended with powdered phenolic resin at an addition rate of 2 . 5 % solids based on oven dry weight of flakes . a wax emulsion at a 1 . 0 % solids addition rate was added to all combinations . all the panels were pressed using mill pressing parameters appropriate for each resin type . the press temperature was 380 ° f . ( 193 ° c .). the initial pressure was 550 psi ( 383 n / cm 2 ). the press cycle times varied from 4 . 0 to 5 . 5 minutes plus a 30 second de - gas period . the target density for the control panels was 40 pcf ( pounds per cubic foot , 0 . 64 g / cm 3 ), and was increased to 42 pcf ( 0 . 67 g / cm 3 ) for the copper ammonium acetate treated panels . the density was increased in the treated panels to maintain an equal wood weight in the finished panels . after pressing the panels were hot stacked for 24 hours prior to mechanical and physical panel property testing . the panels were tested for internal bonding ( ib ), dry and wet strength ( modulus of rupture , mor ), stiffness ( modulus of elasticity , moe ), water absorption ( wa ), thickness swell ( ts ), and wet bending . the results , tables 1a and 1b , indicate a strong dose response between increasing the oil level and the use of copper ammonium acetate complex wood treatment at a 3 . 1 % m / m loading . superior water absorption , thickness swell , enhanced internal bond , and improved wet bending strength were observed . table 1a liquid pf resin : ib , moe , mor , wa ts wet mor ib moe mor wa ts wet mor treatment psi psi psi % % psi ( kpa ) ( mpa ) ( mpa ) % % ( mpa ) control ( no copper 56 . 8 663 , 797 3800 29 . 6 11 . 5 1945 391 . 6 4576 . 7 26 . 2 29 . 6 11 . 5 13 . 4 ammonium acetate complex wood treatment , no oil ) 1 . 25 % oil 63 . 6 762 , 220 4642 26 . 8 8 . 6 1807 438 . 5 5255 . 3 32 . 0 26 . 8 8 . 6 12 . 5 2 . 50 % oil 97 . 2 753 , 322 4489 25 . 3 6 . 7 1987 670 . 1 5194 . 0 30 . 9 25 . 3 6 . 7 13 . 7 5 . 00 % oil 113 . 5 660 , 223 3877 17 . 8 4 . 2 2504 782 . 5 4552 . 1 26 . 7 17 . 8 4 . 2 17 . 3 [ 0082 ] table 1b powder pf resin : ib moe mor wa ts wet mor ib moe mor wa ts wet mor treatment ( psi ) ( psi ) ( psi ) % % ( psi ) ( kpa ) ( mpa ) ( mpa ) % % ( mpa ) control ( no copper 48 . 7 572 , 082 3698 25 . 9 11 . 8 1718 335 . 7 3944 . 4 25 . 5 25 . 9 11 . 8 11 . 8 ammonium acetate complex , no oil ) control with copper 52 . 8 680 , 108 3708 31 . 0 10 . 6 1882 364 . 0 4689 . 2 25 . 6 31 . 0 10 . 6 13 . 0 ammonium acetate complex no oil 1 . 25 % oil 62 . 2 683 , 950 3784 16 . 3 5 . 5 1701 428 . 9 4715 . 7 26 . 1 16 . 3 5 . 5 11 . 7 2 . 50 % oil 81 . 1 855 , 498 4450 16 . 3 4 . 2 1765 559 . 2 5898 . 5 30 . 7 16 . 3 4 . 2 12 . 2 5 . 00 % oil 116 . 4 758 , 729 4655 15 . 6 3 . 7 2354 802 . 5 5231 . 3 32 . 1 15 . 6 3 . 7 16 . 2 to evaluate the decay and termite resistance of the treated panels samples cut from the lab boards were exposed at two field test sites located in hilo , hi . one site provides optimum conditions for wood decay fungi year round , the other provides a severe formosan termite hazard . for the decay testing , a procedure known as the ground proximity test was used . samples 50 × 125 mm × board thickness were placed into test lying flat on top of 100 mm thick concrete blocks in direct contact with the ground . the test samples and concrete blocks were covered with a suspended horticultural shade cloth to allow rain ingress while retarding moisture loss . the amount of decay was measured using a subjective visual rating system after 12 months exposure . a decay rating of ‘ 0 ’ indicates complete destruction of the sample whereas a rating of 100 equates to 100 % sound . data are summarized for liquid pf and powdered pf resin systems in tables 2a and 2b . it is apparent that the copper only and copper + oil treatments provide significant resistance to decay relative to conventional untreated osb samples . for the termite testing a modified version of the set up used for the ground proximity decay test was used . test samples ( 50 × 125 mm × board thickness ) were placed flat side down on the top of open concrete blocks which were in direct contact with the ground . untreated feeder strips were placed between the test samples and into the ground through openings in the concrete blocks to attract termites and to direct them to the test samples . the whole assembly was covered with exterior plywood supported on a treated 1 ″× 6 ″ frame box . inspections were carried out periodically to monitor the performance of the preservatives in the test . a subjective numerical rating system was used to determine the percent volume of sample consumed by termite feeding activities . a termite rating of ‘ 0 ’ indicates complete destruction of the sample whereas a rating of 100 equates to 100 % sound . results are summarized in tables 2c and 2d . the results show that the copper only and copper + oil treatments provide significant protection from formosan termite feeding . untreated osb samples and samples containing oil only were highly susceptible to termite attack . table 2a decay test results field exposure above ground ( ground proximity ) hilo , hi - 12 months exposure liquid pf resin average decay rating treatment ( percent soundness ) control ( no copper ammonium acetate 0 complex , no oil ) control with copper ammonium acetate 78 complex ( comptec ), no oil 1 . 25 % oil + comptec 84 2 . 50 % oil + comptec 88 5 . 00 % oil + comptec 95 1 . 25 % oil only 0 2 . 5 % oil only 0 5 . 0 % oil only 0 [ 0086 ] decay test results field exposure above ground ( ground proximity ) hilo , hi - 12 months exposure powdered pf resin average decay rating treatment ( percent soundness ) control ( no copper ammonium acetate 0 complex , no oil ) control with copper ammonium acetate 78 complex ( comptec ), no oil 1 . 25 % oil + comptec 89 2 . 50 % oil + comptec 89 5 . 00 % oil + comptec 94 1 . 25 % oil only 0 2 . 5 % oil only 0 5 . 0 % oil only 16 [ 0087 ] table 2c termite test results field exposure above ground ( ground proximity ) hilo , hi powdered pf resin average termite rating exposure time ( months ) treatment 5 12 control ( no copper 0 0 ammonium acetate complex , no oil ) control with copper 96 . 3 91 ammonium acetate complex ( comptec ), no oil 1 . 25 % oil + comptec 96 . 7 90 2 . 50 % oil + comptec 96 92 . 8 5 . 00 % oil + comptec 100 95 . 8 1 . 25 % oil only 0 0 2 . 5 % oil only 0 0 5 . 0 % oil only 40 0 [ 0088 ] table 2d termite test results field exposure above ground ( ground proximity ) hilo , hi liquid pf resin average termite rating exposure time ( months ) treatment 5 12 control ( no copper 0 0 ammonium acetate complex , no oil ) control with copper 96 . 3 91 ammonium acetate complex ( comptec ), no oil 1 . 25 % oil + comptec 100 94 . 8 2 . 50 % oil + comptec 100 93 . 8 5 . 00 % oil + comptec 98 . 8 76 . 6 1 . 25 % oil only 0 0 2 . 5 % oil only 0 0 5 . 0 % oil only 8 0 the objective of this study was to determine if the synergistic effects observed with osb would carry over into other composite applications . several sets of medium density fiberboard ( mdf ) panels were manufactured using a lab press and a mixture of northern hardwood fiber . these panels measured 21 inches by 21 inches by ⅜ inch thick ( 53 cm × 53 cm × 1 cm ). fiber as received was rehydrated to approximately 50 % mc ( moisture content ) oven - dry basis to simulate the raw material supply used in conventional mdf manufacturing operations . then the fiber was treated with 3 . 1 % m / m of an active copper ammonium acetate complex wood preservative and 5 % m / m of archer daniels midland gp - 1125 linseed oil . the treated fiber was dried to between 1 - 2 % mc , oven - dry basis . the resulting dried treated fiber was blended with various levels of liquid phenolic resin and 0 . 5 % solids of a wax emulsion . phenolic resin was applied to the treated fiber at 2 , 4 , 6 and 8 % solids levels . a control group of untreated fiber blended with 8 % solids resin and 0 . 5 % solids wax emulsion was manufactured to serve as a reference control . this level of phenolic resin and wax emulsion is typical for the industry . wood composite mats were formed in a deckle box measuring 21 × 21 inches ( 53 × 53 cm ). formed mats were pre - pressed to remove excess air and consolidate the mat to minimize squeeze out of fiber when pressing . this is a common practice in the industry . the mats were pressed at 380 ° f . ( 193 ° c .) for a total of 5 . 5 minutes − five minutes under pressure and a 30 second de - gas . the initial pressure was 550 psi ( 383 n / cm 2 ) on the mat , decreasing to a cook pressure of 200 psi ( 139 n / cm 2 ), and a reduction to 0 psi ( 0 n / cm 2 ) during the de - gas phase . the target thickness was ⅜ inch ( 1 cm ) with a target density of 62 pcf ( 1 g / cm 3 ). the pressed panels were allowed to hot stack 24 hours prior to mechanical and physical panel property testing . the panels were evaluated for internal bond , water absorption , thickness swell , strength , and stiffness . with osb , having observed the influence on mechanical properties of the oil / copper ammonium acetate complex mixture , it was determined to gradually decrease the level of phenolic resin used . this was done to gauge the impact of the resin level upon the mechanical and physical properties of osb . knowing the industry norm is as listed above , one would expect the properties of the resulting panels to fall off as the resin level was decreased . however , that was not the case . given the fact that it is standard practice within the mdf manufacturing industry to use pf resin loadings of 8 %, the results provided as table 3 are remarkable . it is apparent that that the oil / copper ammonium acetate complex combination can replace most , if not all , the phenolic resin in the finished panels . panels containing a copper ammonium acetate complex and oil but no conventional resin possessed similar or superior properties over the controls . the presence of an oil and a copper ammonium acetate complex appears to produce panels with superior properties at any given resin level . the dimensional stability and water absorption characteristics of the mdf panels were significantly improved when the oil / copper ammonium acetate complex treatment was utilized regardless of resin level . while excellent results were observed adding linseed oil and copper ammonium acetate complex wood treatment to the green furnish prior to drying , it was hypothesized that similar results could occur if the oil was added to the blender at the same time as the resin and wax . the copper ammonium acetate complex wood treatment is desirably added to the green strands prior to drying since the increase in moisture content associated with the water borne preservative might not be conducive to a blender application . in the manufacture of osb , wax emulsions are typically incorporated into the furnish at an addition rate of 1 . 0 % solids . with such a low rate of addition , optimizing coverage and distribution on the entire volume of furnish can be a challenge . one of the potential benefits of adding the linseed oil at the same time as either the wax or liquid resin is that the combined volumes of these components would be increased . this would result in better coverage and distribution of the materials . as a consequence there is the potential to improve the panel properties by improving distribution alone . to evaluate the likelihood of this occurring , archer daniel midland gp - 1125 linseed oil was added to a commercial wax emulsion , borden &# 39 ; s ew 58 - s . the wax and linseed oil were mixed in a ratio of 50 : 50 based on solids of each material . this mixture was thoroughly mixed prior to application through a coil spinning disc atomizer to the strands being tumbled in a laboratory batch blender . the strands used for the study were primarily aspen with a percentage of white birch and red pine mixed in . the strands were hydrated to approximately 50 % moisture content , then treated with 3 . 1 % m / m of an active copper ammonium acetate complex wood treatment , and dried to approximately 4 % moisture content . the treated strands were blended with 2 . 5 % of powdered phenolic resin and various loadings of the blended oil and wax . a total of four groups of panels were produced for this study . a control group with the treated strands and a loading of 1 . 0 % solids wax emulsion was manufactured for a reference . the three experimental combinations were 1 . 0 % solids of the wax / oil mixture , 2 . 0 % solids wax oil mixture , and 4 . 0 % solids of the wax oil mixture . the blended furnish was formed into 21 - inch by 21 - inch inch ( 53 cm × 53 cm ) mats . the target thickness was 12 inch ( 1 . 2 cm ) with a target density of 42 pcf ( 0 . 67 g / cm 3 ). the panels were pressed at 400 ° f . ( 204 ° c .) with a total press time of 5 . 5 minutes . the panels were allowed to hot stack overnight prior to cutting into test specimens . since the wax and oil levels were elevated and the oil was not partially cured as in the previous examples , the internal bond testing was paramount to assess what if any effect the conditions used would have on bonding . wet bending assessments were carried out to gauge the impact the perceived increase in water resistance would have on maintaining strength after exposure . water absorption and thickness swell were measured to determine potential improvements . the internal bond results testing indicates that we did not see as large an increase in strength as we observed in previous work where the oil was added to the green flakes . however , the oil loading was only 2 . 0 % versus the 5 . 0 % in the examples 1 and 2 . regardless , there was a dose response in internal bond strength : as the oil content increased from 0 . 5 % to the maximum of 2 . 0 % the internal bond value improved and was approximately double than that of the controls . similar results in improved wet bending properties were observed . the 2 . 0 % and 4 . 0 % overall dosage had significantly higher wet bending strength than the controls or 1 . 0 % group . as the percentage of oil and wax increased , the thickness swell and water absorption values decreased . at the 4 . 0 % combination the thickness swell was reduced to 5 . 2 % based upon the original thickness of the panel . the previous examples demonstrate that there is a strong synergy between reactive agricultural based oils and copper ammonium acetate complex wood treatment . when both components are used together to treat green or dry furnish there tends to be an improvement in strength of the bonds formed between individual particles making up the wood based composite . it is hypothesized earlier that there appears to be a chemical reaction between the oil and copper ammonium acetate complex wood treatment that effectively epoxidizes the linseed oil into a strong bonding agent . while the increase in dimensional stability produced by the use of oil and copper ammonium acetate complex wood treatment in combination is attractive for composite panel products , the observed improvement in resin bond suggests that there may be additional benefits for a composite panel manufacturing processes . one is the manufacture of superior panel products , and the other is the development of a whole new resin system that could replace a percentage or all of the synthetic resins currently being used by the composite board industry . typically , when oriented strandboard mats are pressed under heat and pressure in the absence of resin , the resulting panel has no strength or integrity . the flakes can be separated freely . the flakes would appear to be the same after pressing as before blending . the objective of this study was to investigate the bonding efficacy of the linseed oil / copper ammonium acetate complex wood treatment reaction . essentially , we were trying to determine if it is possible to manufacture composite panels using little or no synthetic resin , but relying solely on the bond produced by the interaction of the oil and preservative . for this study , aspen strands containing a small percentage of white birch and red pine were rehydrated from dry to approximately 50 % moisture content . the wet strands were blended with a mixed solution of copper ammonium acetate complex wood treatment and archer daniels midland &# 39 ; s gp - 1125 linseed oil . the final addition rate of copper ammonium acetate complex wood treatment in the panel was 3 . 1 % m / m active and the addition rate of linseed oil was 5 . 0 % m / m active . the strands were dried to approximately 4 % moisture content after treatment . one set of the strands was blended with a liquid phenolic resin at a 0 . 5 % solids addition rate . for the other set the resin blending step was skipped . mats ( 21 - inch by 21 - inch inch , 53 cm × 53 cm ) were formed with the two sets of oil / copper ammonium acetate complex wood treatment treated strands . mats were pressed in a laboratory press to a target panel thickness of ½ inch ( 1 . 2 cm ) with a target density of 42 pcf ( 0 . 67 g / cm 3 ). panels were pressed at 400 ° f . ( 204 ° c .) for a total of 7 . 5 minutes . internal bond measurements were made on samples of the panels without synthetic resin immediately after pressing . additional internal bond measurements and dry static bending assessments were made on test specimens after hot stacking overnight . coming out of the press the panels made without synthetic resin appeared to be similar in appearance and behavior to conventional panels bonded with conventional resin systems . the no - resin panels appeared to be strong and stiff to the touch , and when the panels were struck a hard solid sound was returned . the internal bond measurements of the panels made with no resin ( table 5 ) show that a suitable oriented strandboard panel can be produced . the internal bond values on panels without resin , straight out of the press ( i . e . hot ), averaged 34 . 2 psi ( 23 . 8 n / cm 2 ). these values were similar in magnitude to the internal bond values of some of the control panels produced in the earlier examples . after hot stacking overnight , the internal bond value in these same panels increased to an average of 38 . 6 psi ( 26 . 9 n / cm 2 ). the ib values for test panels containing 0 . 5 % resin solids exhibited an average internal bond of 49 . 4 psi ( 34 . 43 n / cm 2 ). the strength and stiffness of the no - resin panel was slightly better than the panel containing 0 . 5 % resin solids . based on the mor and moe data , both sets of panels ( resin and no resin ) meet acceptance criteria for randomly produced oriented strandboard . the data clearly indicates that there is a strong reaction between the linseed oil and copper ammonium acetate complex wood treatment that can be exploited to produce acceptable strandboard panels without the use of synthetic resins . in the previous examples the benefits of a combination of linseed oil and preservative in the manufacture of oriented strand board were demonstrated . the intent of this study was to investigate the synergy of other agricultural oils and comptec preservative on osb panel properties . results for canola , rapeseed , soy and tung oils are presented relative to linseed oil . seven panel sets were produced . treatment of flakes was achieved using a coil type atomizer and a rotary blender . green flakes ( 45 % mc ) were treated with comptec preservative to achieve a 1 % a . i . loading ( oven dry weight of flakes basis ) and a 5 % solids basis with different oils ( canola ( archer daniel midland 81 - 060 - 0 ), rapeseed , soy ( adm golden chef 104 - 051 ), linseed ( adm gp - 1125 ) and tung ) allowing sufficient dwell time for diffusion . treated flakes were then dried to a nominal 2 % moisture content . flakes without treatments and flakes treated with 1 % m / m a . i . comptec alone were prepared as reference controls . face and core liquid formaldehyde resin was added to each batch of the dry treated furnish at an addition rate of 3 . 5 % along with a petroleum based wax emulsion borden ew58s ( 1 % solids oven dry weight of wood flakes basis ). panels were hand formed in a random orientation on mats ( 21 - inch by 21 - inch inch , 53 cm × 53 cm ). mats were pressed in a laboratory press to a target panel thickness of 12 inch ( 1 . 2 cm ) with a target density of 42 pcf ( 0 . 67 g / cm 3 ). panels were pressed at 380 ° f . ( 204 ° c .) for a total of 6 minutes . manufactured panels were tested for internal bond , water absorption , thickness swell and wet modulus of rupture . summarized results are tabulated in table 6 . as the results in table 6 illustrate the internal bond ( ib ) values for all treated panels are superior to the ib values untreated control panels . the comptec only treatment yielded an ib of 63 . 5 psi while the addition of tung and linseed oils to the comptec enhanced the ib values considerably 120 and 93 . 2 psi respectively . all treatments provided superior water absorption and thickness swell values relative to the untreated controls . rapeseed oil in combination with comptec proved to be the most efficacious of the series with absorption values of 13 % and swelling of 4 . 1 % respectively . the wet mor values of the all treated panels were equivalent to the mor values of the untreated controls indicating that the strength characteristics of the treated boards were not affected by the different treatments . in conclusion it is apparent that a combination of comptec with a range of different agricultural based oils can enhance the performance characteristics of oriented strand board .