JPH11124556A - Preparation of wood adhesive - Google Patents
Preparation of wood adhesiveInfo
- Publication number
- JPH11124556A JPH11124556A JP29011797A JP29011797A JPH11124556A JP H11124556 A JPH11124556 A JP H11124556A JP 29011797 A JP29011797 A JP 29011797A JP 29011797 A JP29011797 A JP 29011797A JP H11124556 A JPH11124556 A JP H11124556A
- Authority
- JP
- Japan
- Prior art keywords
- phenol
- formaldehyde
- resin
- molar ratio
- adhesive
- 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.)
- Pending
Links
- 239000000853 adhesive Substances 0.000 title claims abstract description 40
- 230000001070 adhesive effect Effects 0.000 title claims abstract description 40
- 239000002023 wood Substances 0.000 title claims description 9
- 238000002360 preparation method Methods 0.000 title description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims abstract description 103
- 239000005011 phenolic resin Substances 0.000 claims abstract description 43
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229920005989 resin Polymers 0.000 claims abstract description 24
- 239000011347 resin Substances 0.000 claims abstract description 24
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 claims abstract description 21
- 229920001568 phenolic resin Polymers 0.000 claims abstract description 21
- 239000003054 catalyst Substances 0.000 claims abstract description 6
- 229920003987 resole Polymers 0.000 claims abstract description 5
- 239000000203 mixture Substances 0.000 claims description 4
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 claims 1
- 150000002989 phenols Chemical class 0.000 abstract description 3
- 235000019256 formaldehyde Nutrition 0.000 abstract 10
- 238000009833 condensation Methods 0.000 abstract 1
- 230000005494 condensation Effects 0.000 abstract 1
- 238000002156 mixing Methods 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 18
- 239000011120 plywood Substances 0.000 description 16
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 9
- 239000007788 liquid Substances 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 8
- 238000010992 reflux Methods 0.000 description 8
- 229920003180 amino resin Polymers 0.000 description 6
- 235000013312 flour Nutrition 0.000 description 6
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 6
- 235000011121 sodium hydroxide Nutrition 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 241000218652 Larix Species 0.000 description 4
- 235000005590 Larix decidua Nutrition 0.000 description 4
- 239000004606 Fillers/Extenders Substances 0.000 description 3
- 239000004067 bulking agent Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 3
- 239000011122 softwood Substances 0.000 description 3
- ZHNUHDYFZUAESO-UHFFFAOYSA-N Formamide Chemical compound NC=O ZHNUHDYFZUAESO-UHFFFAOYSA-N 0.000 description 2
- 229920000877 Melamine resin Polymers 0.000 description 2
- 239000003518 caustics Substances 0.000 description 2
- 239000011121 hardwood Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 1
- 239000004640 Melamine resin Substances 0.000 description 1
- 229930040373 Paraformaldehyde Natural products 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000012790 adhesive layer Substances 0.000 description 1
- 150000004982 aromatic amines Chemical class 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229930003836 cresol Natural products 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- IVJISJACKSSFGE-UHFFFAOYSA-N formaldehyde;1,3,5-triazine-2,4,6-triamine Chemical compound O=C.NC1=NC(N)=NC(N)=N1 IVJISJACKSSFGE-UHFFFAOYSA-N 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 231100000206 health hazard Toxicity 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- CUONGYYJJVDODC-UHFFFAOYSA-N malononitrile Chemical compound N#CCC#N CUONGYYJJVDODC-UHFFFAOYSA-N 0.000 description 1
- JDSHMPZPIAZGSV-UHFFFAOYSA-N melamine Chemical compound NC1=NC(N)=NC(N)=N1 JDSHMPZPIAZGSV-UHFFFAOYSA-N 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229920003986 novolac Polymers 0.000 description 1
- 229920002866 paraformaldehyde Polymers 0.000 description 1
- 229920002037 poly(vinyl butyral) polymer Polymers 0.000 description 1
- 239000011134 resol-type phenolic resin Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229920001864 tannin Polymers 0.000 description 1
- 235000018553 tannin Nutrition 0.000 description 1
- 239000001648 tannin Substances 0.000 description 1
- 125000002256 xylenyl group Chemical class C1(C(C=CC=C1)C)(C)* 0.000 description 1
Landscapes
- Veneer Processing And Manufacture Of Plywood (AREA)
- Phenolic Resins Or Amino Resins (AREA)
- Adhesives Or Adhesive Processes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は木材用フェノール・
ホルムアルデヒド樹脂接着剤(以下、フェノール・ホル
ムアルデヒド樹脂をフェノール樹脂という)に関し、詳
しくは低温速硬化であり低ホルムアルデヒド化されたフ
ェノール樹脂接着剤に関する。TECHNICAL FIELD The present invention relates to a phenol for wood.
The present invention relates to a formaldehyde resin adhesive (hereinafter, phenol / formaldehyde resin is referred to as a phenol resin), and more particularly, to a phenol resin adhesive which is a low-temperature fast-curing low-formaldehyde resin.
【0002】[0002]
【従来の技術】近年、広葉樹資源の入手難から、合板材
料として針葉樹資源の利用が考えられている。しかし、
メラミン・ホルムアルデヒド樹脂、尿素・ホルムアルデ
ヒド樹脂で代表されるアミノ系樹脂接着剤を接着剤とし
たものでは、接着性、耐久性、安定性などの点で不十分
であり、針葉樹を原料とした合板の信頼性を高めていく
ためには接着性、耐久性、安定性に優れているフェノー
ル樹脂系接着剤を用いるのが良いとされている。2. Description of the Related Art In recent years, utilization of softwood resources as a plywood material has been considered due to difficulty in obtaining hardwood resources. But,
The use of amino resin adhesives represented by melamine / formaldehyde resins and urea / formaldehyde resins as adhesives is insufficient in terms of adhesiveness, durability and stability. It is said that it is better to use a phenolic resin-based adhesive excellent in adhesiveness, durability and stability in order to increase reliability.
【0003】従来のフェノール樹脂接着剤は、アミノ系
樹脂接着剤と比較して、合板を製造する際の熱圧締(プ
レス)に際し、高温、長時間を要し、これがために作業
性の低下、プレス後の製品の厚み減り、表面劣化の原因
となっている。Conventional phenolic resin adhesives require a high temperature and a long time for hot pressing (pressing) in the production of plywood as compared with amino resin adhesives, thereby reducing workability. This causes a reduction in the thickness of the product after pressing and surface deterioration.
【0004】また、ホルマリンの室内汚染による健康被
害の問題がクローズアップされ、合板に対するJAS規
格におけるホルムアルデヒド放散量の規格として、F−
1グレード(ホルムアルデヒド放散量(以下、F放散量
という):0.5ppm以下)が要求されている。[0004] In addition, the problem of health hazard due to indoor contamination of formalin has been highlighted, and as a standard for formaldehyde emission in the JAS standard for plywood, F-
One grade (formaldehyde emission (hereinafter referred to as F emission): 0.5 ppm or less) is required.
【0005】フェノール樹脂系接着剤の低温速硬化の方
法としては、ホルムアルデヒドとフェノールのモル比
(以下、F/Pモル比という。)を2.5〜3.0に
し、レゾルシノールを添加剤とすれば、ある程度効果の
得られることは知られているが、この方法では、生産し
た合板のF放散量は20ppmを越え、且つ、糊液の可
使時間が極めて短く実用的ではない。As a method for rapidly curing a phenolic resin-based adhesive at a low temperature, the molar ratio of formaldehyde to phenol (hereinafter referred to as F / P molar ratio) is set to 2.5 to 3.0, and resorcinol is used as an additive. Although it is known that some effect can be obtained, in this method, the amount of F emitted from the produced plywood exceeds 20 ppm and the potable liquid has a very short pot life, which is not practical.
【0006】次に、フェノール樹脂のF/Pモル比を
2.0〜2.5としパラホルムアルデヒドを添加するこ
とにより速硬化化する試みがなされており、フェノール
樹脂のモル比が高くなればより速硬化となり、接着力が
安定するが、上記のモル比の範囲ではF放散量がF−1
のグレードを満たすのは困難である。Next, attempts have been made to set the F / P molar ratio of the phenol resin to 2.0 to 2.5 and to rapidly cure the mixture by adding paraformaldehyde. Fast curing and stable adhesive strength, but the amount of F emission is F-1 in the above molar ratio range.
It is difficult to meet the grade.
【0007】一方、F/Pモル比を2.0以下とした場
合はF放散量はF−1を満たすもののアミノ樹脂接着剤
と同等の熱圧条件下では接着力の安定性に欠ける。On the other hand, when the F / P molar ratio is 2.0 or less, the amount of F emission satisfies F-1, but the stability of adhesive strength is lacking under the same heat and pressure conditions as the amino resin adhesive.
【0008】また、硬化助剤として、レゾルシノール、
ホルムアミド、マロンニトリル、芳香族アミン、ノボラ
ックなどが提案されているが、多量に添加しないと効果
が小さく、多量に添加すると糊液の粘度上昇が極めて速
くなり、生産性の点で問題があった。Further, resorcinol, a curing aid,
Formamide, malononitrile, aromatic amine, novolak, etc. have been proposed, but the effect is small if not added in a large amount, and if added in a large amount, the viscosity rise of the size liquid becomes extremely fast, and there is a problem in terms of productivity. .
【0009】[0009]
【発明が解決しようとする課題】本発明は、生産性を従
来の広葉樹材料に対するアミノ系接着剤の生産性を維持
しつつ、針葉樹単板に対する優れた接着性を発現し、合
板から発するホルムアルデヒド臭を低減した木材用低温
速硬化・低ホルマリン臭合板用レゾール型フェノール樹
脂接着剤を提供することにある。DISCLOSURE OF THE INVENTION The present invention provides a formaldehyde odor emitted from plywood while exhibiting excellent adhesiveness to softwood veneers while maintaining productivity of an amino-based adhesive to conventional hardwood materials. It is an object of the present invention to provide a resol type phenolic resin adhesive for low-temperature fast-curing and low-formalin odor plywood for wood, which has reduced odor.
【0010】[0010]
【課題を解決するための手段】本発明は、速硬化成分で
ある高モル比のフェノール樹脂(A)とホルムアルデヒ
ドキャッチャー効果を付与するために、低モル比のフェ
ノール樹脂(B)とをブレンドすることを特徴とする。
これにより得られたフェノール樹脂接着剤が、汎用のフ
ェノール樹脂接着剤の140〜150℃、50秒/mm
という高温、長時間の加熱条件に比べ、アミノ樹脂接着
剤の加熱条件とほぼ同等の120〜125℃、25〜3
0秒/mmという低温、短時間でも十分な接着性を得つ
つ、合板のF放散量の低減が可能となる。According to the present invention, a high-molar ratio phenol resin (A), which is a fast-curing component, is blended with a low-molar ratio phenol resin (B) to impart a formaldehyde catcher effect. It is characterized by the following.
The phenolic resin adhesive thus obtained is a general-purpose phenolic resin adhesive at 140 to 150 ° C. and 50 seconds / mm.
120-125 ° C, 25-3 which is almost the same as the heating condition of the amino resin adhesive,
It is possible to reduce the amount of F emitted from the plywood while obtaining sufficient adhesiveness even at a low temperature of 0 sec / mm and for a short time.
【0011】即ち、F/Pモル比を2.2〜3.0と
し、アルカリ性触媒下で通常還流下もしくは85℃以上
の温度で所定の粘度まで反応せしめ高モル比のフェノー
ル樹脂接着剤(A)を得る。更に、F/Pモル比を1.
1〜1.5とし、塩基性触媒下で通常還流下もしくは8
5℃以上の温度で所定の粘度にまで反応せしめ低モル比
のフェノール樹脂(B)を得る。配合については、高モ
ル比の樹脂(A)100重量部に対して、低モル比の樹
脂(B)を10〜60重量部を添加することにより、ア
ミノ樹脂系接着剤と同等の加熱条件で、且つ、アミノ樹
脂系接着剤では十分な耐久性が得られない針葉樹単板を
使用して、同等の接着性能を有し、そしてF放散量がF
−1グレードを満たすことができる。That is, the F / P molar ratio is set to 2.2 to 3.0, and the mixture is reacted to a predetermined viscosity under an alkaline catalyst usually under reflux or at a temperature of 85 ° C. or higher, and a phenol resin adhesive (A Get) Further, the F / P molar ratio is set to 1.
1 to 1.5, usually under reflux or 8 under a basic catalyst.
The reaction is allowed to proceed to a predetermined viscosity at a temperature of 5 ° C. or higher to obtain a phenol resin (B) having a low molar ratio. About the compounding, by adding 10 to 60 parts by weight of the resin (B) having a low molar ratio to 100 parts by weight of the resin (A) having a high molar ratio, under the same heating conditions as the amino resin adhesive. In addition, using a softwood veneer, which does not provide sufficient durability with an amino resin-based adhesive, has the same adhesive performance, and the F emission amount is F
-1 grade can be satisfied.
【0012】好ましくは、本発明は、ホルムアルデヒド
とフェノール類のモル比を2.2〜3.0とし、通常還
流下もしくは85℃以上の温度で、25℃における不揮
発分55〜60%でのB型粘度計の粘度を6.0〜1
5.0psまで反応させ高モル比のフェノール樹脂接着
剤(A)を得る。ついで、F/Pモル比を1.1〜1.
5とし、通常還流下もしくは85℃以上の温度で、25
℃における不揮発分50〜55%でのB型粘度計の粘度
を0.5〜2.0psとなるまで反応させ低モル比のフ
ェノール樹脂(B)を得る。高モル比のフェノール樹脂
(A)の粘度を限定する理由は、6.0ps未満では以
下では十分な速硬化性が期待できず、15.0psの粘
度となると作業性が悪くなる。次に、低モル比のフェノ
ール樹脂(B)の粘度が0.5psでは反応の進行が不
十分で、2.0psではホルムアルデヒドキャッチャー
効果が十分に得られない。Preferably, in the present invention, the molar ratio of formaldehyde to phenols is 2.2 to 3.0, and the B content at 55 to 60% of the non-volatile content at 25 ° C. usually under reflux or at a temperature of 85 ° C. or more. The viscosity of the viscometer is 6.0 to 1
The reaction is performed up to 5.0 ps to obtain a phenolic resin adhesive (A) having a high molar ratio. Then, the F / P molar ratio was adjusted to 1.1 to 1.
5, 25 ° C under normal reflux or at a temperature of 85 ° C or higher.
The phenol resin (B) having a low molar ratio is obtained by reacting the viscosity of the B-type viscometer at a non-volatile content of 50 to 55% at a temperature of 0.5 to 2.0 ps. The reason for limiting the viscosity of the phenolic resin (A) having a high molar ratio is that if the viscosity is less than 6.0 ps, sufficient rapid curability cannot be expected below, and if the viscosity becomes 15.0 ps, the workability deteriorates. Next, when the viscosity of the phenol resin (B) having a low molar ratio is 0.5 ps, the reaction proceeds insufficiently, and when the viscosity is 2.0 ps, a sufficient formaldehyde catcher effect cannot be obtained.
【0013】フェノール樹脂に使用するフェノール類と
してはフェノール、クレゾール、キシレノール、レゾル
シノール等が使用可能である。As phenols used for the phenol resin, phenol, cresol, xylenol, resorcinol and the like can be used.
【0014】本発明のフェノール樹脂接着剤は、ホルム
アルデヒドとフェノールとを反応させたフェノール樹脂
を主体としたものであるが、タンニン、リグニン、ボリ
ビニルブチラール、エチレングリコール、ジエチレング
リコールなどで一部変性した変性樹脂あってもよい。な
お、これらの変性剤はフェノール樹脂(A)、(B)の
いずれの樹脂に配合してもよく、冷却時に配合すること
が好ましい。The phenolic resin adhesive of the present invention is mainly composed of a phenolic resin obtained by reacting formaldehyde and phenol, and is partially modified with tannin, lignin, polyvinyl butyral, ethylene glycol, diethylene glycol or the like. There may be resin. In addition, these modifiers may be blended with any of the phenolic resins (A) and (B), and are preferably blended during cooling.
【0015】アルカリ性触媒として苛性ソーダを使用す
る場合、その触媒量は特に規定されないが、水溶性を良
好とするため、苛性ソーダとフェノールのモル比(以
下、苛性/Pモル比という。)が0.1以上が望まし
く、さらに0.5を越えないことが望ましい。苛性/P
モル比が0.5を越えると接着剤層の耐水性が低化する
ようになる。When caustic soda is used as an alkaline catalyst, the amount of the catalyst is not particularly limited, but the molar ratio of caustic soda to phenol (hereinafter, referred to as caustic / P molar ratio) is 0.1 in order to improve water solubility. The above is desirable, and it is more desirable that the value does not exceed 0.5. Caustic / P
If the molar ratio exceeds 0.5, the water resistance of the adhesive layer will decrease.
【0016】上記の様にして得た高モル比のフェノール
樹脂(A)100重量部に対して、低モル比のフェノー
ル樹脂(B)を10〜80重量部好ましくは10〜60
重量部添加し、小麦粉などの増量剤を添加することによ
って接着剤糊液を得る。低モル比のフェノール樹脂
(B)の添加量が10重量部より少ないとホルムアルデ
ヒドキャッチャー効果が十分に発現せず、80重量部よ
り多くすると接着力の安定性に欠けるために好ましくな
い。With respect to 100 parts by weight of the phenolic resin (A) having a high molar ratio obtained as described above, 10 to 80 parts by weight, preferably 10 to 60 parts by weight, of the phenolic resin (B) having a low molar ratio is used.
The adhesive paste liquid is obtained by adding parts by weight and adding a bulking agent such as flour. If the amount of the phenolic resin (B) having a low molar ratio is less than 10 parts by weight, the formaldehyde catcher effect is not sufficiently exhibited, and if it is more than 80 parts by weight, the stability of the adhesive strength is not preferable.
【0017】本発明の接着剤には、充填剤、増量剤、
水、硬化促進剤などを必要に応じて添加混合することも
可能である。The adhesive of the present invention includes a filler, a bulking agent,
Water, a hardening accelerator and the like can be added and mixed as necessary.
【0018】[0018]
【実施例】次に、本発明を実施例に基づき説明する。Next, the present invention will be described based on embodiments.
【0019】フェノール樹脂製造例1 予め、フェノール94.1重量部と37%ホルムアルデ
ヒド210.8重量部(F/Pモル比=2.6)及び3
0%苛性ソーダを55重量部仕込み、還流条件下で40
分反応させさらに85℃にてB型粘度計にて不揮発分5
2%での粘度が約8psとなるまで反応させた。その
後、水を添加し樹脂粘度を約2psに調整してレゾール
型フェノール樹脂(A1)を得る。Phenol Resin Production Example 1 94.1 parts by weight of phenol and 210.8 parts by weight of 37% formaldehyde (F / P molar ratio = 2.6) and 3
55% by weight of 0% caustic soda was charged and 40% under reflux conditions.
And a non-volatile content of 5 with a B-type viscometer at 85 ° C.
The reaction was continued until the viscosity at 2% became about 8 ps. Thereafter, water is added to adjust the resin viscosity to about 2 ps to obtain a resol-type phenol resin (A1).
【0020】フェノール樹脂製造例2 予め、フェノール94.1重量部と37%ホルムアルデ
ヒド243.2重量部(F/Pモル比=3.0)及び3
0%苛性ソーダを55重量部仕込み、還流条件下で40
分反応させさらに85℃にてB型粘度計にて不揮発分5
5%での粘度が約12psとなるまで反応させた。その
後、水及びエチレングリコールを添加し樹脂粘度を約2
psに調整してレゾール型フェノール樹脂(A2)を得
る。Phenol Resin Production Example 2 94.1 parts by weight of phenol and 243.2 parts by weight of 37% formaldehyde (F / P molar ratio = 3.0) and 3
55% by weight of 0% caustic soda was charged and 40% under reflux conditions.
And a non-volatile content of 5 with a B-type viscometer at 85 ° C.
The reaction was continued until the viscosity at 5% became about 12 ps. Thereafter, water and ethylene glycol were added to reduce the resin viscosity to about 2
By adjusting to ps, a resol type phenol resin (A2) is obtained.
【0021】フェノール樹脂製造例3 予め、フェノール94.1重量部と37%ホルムアルデ
ヒド97.3重量部(F/Pモル比=1.2)及び30
%苛性ソーダ55重量部仕込み、還流条件下で80分反
応させ、更に85℃にて樹脂粘度が約1PSとなるまで
反応させレゾール型フェノール樹脂(B1)を得る。Preparation Example 3 of Phenol Resin 94.1 parts by weight of phenol and 97.3 parts by weight of 37% formaldehyde (F / P molar ratio = 1.2)
55 parts by weight of caustic soda are reacted under reflux conditions for 80 minutes, and further reacted at 85 ° C. until the resin viscosity becomes about 1 PS to obtain a resol type phenol resin (B1).
【0022】フェノール樹脂製造例4 予め、フェノール94.1重量部と37%ホルムアルデ
ヒド162.2重量部(F/Pモル比=2.0)及び3
0%苛性ソーダ55重量部仕込み、還流条件下で50分
反応させ、更に85℃にて樹脂粘度が約8psとなるま
で反応させた。その後、水及びエチレングリコールを添
加し樹脂粘度を約2psに調整してレゾール型フェノー
ル樹脂(C)を得た。これらの製造例において、いずれ
の場合も、樹脂固形分は約48%となる様に調整してい
る。Phenol Resin Production Example 4 94.1 parts by weight of phenol and 162.2 parts by weight of 37% formaldehyde (F / P molar ratio = 2.0) and 3
55% by weight of 0% caustic soda was charged and reacted under reflux conditions for 50 minutes, and further reacted at 85 ° C. until the resin viscosity became about 8 ps. Thereafter, water and ethylene glycol were added to adjust the resin viscosity to about 2 ps, thereby obtaining a resol type phenol resin (C). In each of these production examples, the resin solid content was adjusted to be about 48% in each case.
【0023】このようにして得たフェノール樹脂を使用
して、以下の実施例の通りに接着剤糊液を調製し、合板
を作成した。Using the phenolic resin thus obtained, an adhesive paste solution was prepared as in the following examples to prepare plywood.
【0024】実施例1 フェノール樹脂製造例1で得られたフェノール樹脂(A
1)100重量部とフェノール樹脂製造例3で得られた
フェノール樹脂(B1)60重量部とを混合攪拌し、増
量剤として小麦粉16重量部を配合し糊液を得、1.8
mm厚のカラマツの単板を5plyにて合板を作成し
た。成形条件は糊塗工量:28g/尺、冷圧条件:10
kg/cm2、加熱条件:10kg/cm2、120
℃、25秒/mmで実施した。Example 1 Phenol resin (A)
1) 100 parts by weight and 60 parts by weight of the phenolic resin (B1) obtained in Phenol Resin Production Example 3 were mixed and stirred, and 16 parts by weight of flour was added as an extender to obtain a paste liquid.
Plywood was prepared from 5 mm thick larch veneers at 5 ply. The molding conditions were as follows: glue coating amount: 28 g / size, cold pressure condition: 10
kg / cm2, heating condition: 10 kg / cm2, 120
C., 25 seconds / mm.
【0025】実施例2 フェノール樹脂製造例2で得られたフェノール樹脂(A
2)100重量部とフェノール樹脂製造例3で得られた
フェノール樹脂(B1)30重量部とを混合攪拌し、増
量剤として小麦粉13重量部を配合し糊液を得、実施例
1と同様にして1.8mm厚のカラマツの単板を5pl
yにて合板を作成した。Example 2 Phenol Resin (A)
2) 100 parts by weight and 30 parts by weight of the phenol resin (B1) obtained in Phenol Resin Production Example 3 were mixed and stirred, and 13 parts by weight of flour was added as an extender to obtain a size liquid, as in Example 1. Larch veneer 1.8 mm thick with 5 pl
A plywood was prepared with y.
【0026】比較例1 フェノール樹脂製造例1で得られたフェノール樹脂(A
1)100重量部、増量剤として小麦粉10重量部を配
合し糊液を得、1.8mm厚のカラマツの単板を5pl
yにて合板を作成した。Comparative Example 1 The phenolic resin (A
1) 100 parts by weight and 10 parts by weight of flour as a bulking agent were blended to obtain a size liquid, and 5 pl of a 1.8 mm-thick larch veneer was prepared.
A plywood was prepared with y.
【0027】比較例2 フェノール樹脂製造例4で得られたフェノール樹脂接着
剤(C)100重量部、増量剤として小麦粉10重量部
を配合し糊液を得、1.8mm厚のカラマツの単板を5
plyにて合板を作成した。Comparative Example 2 100 parts by weight of the phenolic resin adhesive (C) obtained in Production Example 4 of phenolic resin and 10 parts by weight of flour as an extender were blended to obtain a paste liquid, and a larch veneer having a thickness of 1.8 mm was used. 5
A plywood was prepared by ply.
【0028】比較例3 ホルムアルデヒドとメラミンのモル比を0.6のメラミ
ン樹脂接着剤を100重量部、小麦粉を10重量部配合
し、糊液を得、実施例と同様にし合板を得た。Comparative Example 3 100 parts by weight of a melamine resin adhesive having a molar ratio of formaldehyde to melamine of 0.6 and 10 parts by weight of flour were blended to obtain a paste liquid, and a plywood was obtained in the same manner as in Example.
【0029】糊液を調製するための配合を表1にまとめ
た。The formulations for preparing the size liquid are summarized in Table 1.
【表1】 [Table 1]
【0030】得られた各合板について、常態及び特類の
接着力と放散ホルムアルデヒド量の評価を実施した。そ
の結果は表2の通りであった。Each of the obtained plywoods was evaluated for normal and special adhesive strength and the amount of formaldehyde emitted. Table 2 shows the results.
【表2】 [Table 2]
【0031】[0031]
【発明の効果】本発明の木材用接着剤は、従来のアミノ
系樹脂接着剤生産性を維持しつつ、アミノ系接着剤では
達成しえなかった特類合板の接着強度を持ち、ホルムア
ルデヒド放散量のJAS規格においてF−1グレードを
満たす合板を得ることができる。The wood adhesive of the present invention has the adhesive strength of a special kind of plywood that cannot be achieved with an amino-based adhesive while maintaining the productivity of the conventional amino-based resin adhesive. A plywood satisfying the F-1 grade in the JAS standard can be obtained.
Claims (3)
とアルデヒド類を縮合させて得られるレゾール型フェノ
ール樹脂において、フェノールとホルムアルデヒドのモ
ル比を2.0〜3.0にて反応させたフェノール・ホル
ムアルデヒド樹脂(A)と、フェノールとホルムアルデ
ヒドのモル比を1.1〜1.5にて反応させたフェノー
ル・ホルムアルデヒド樹脂(B)をブレンドすることを
特徴とする木材用接着剤。1. A resol type phenol resin obtained by condensing a phenol and an aldehyde in the presence of an alkaline catalyst, wherein the phenol / formaldehyde is reacted at a molar ratio of phenol to formaldehyde of 2.0 to 3.0. An adhesive for wood, wherein the resin (A) is blended with a phenol-formaldehyde resin (B) obtained by reacting phenol and formaldehyde at a molar ratio of 1.1 to 1.5.
比率がフェノール・ホルムアルデヒド樹脂(A)100
重量部に対し、フェノール・ホルムアルデヒド樹脂
(B)10〜80重量部である請求項1記載の木材用接
着剤。2. The blend ratio for obtaining the wood adhesive is phenol / formaldehyde resin (A) 100.
The wood adhesive according to claim 1, wherein the phenol / formaldehyde resin (B) is used in an amount of 10 to 80 parts by weight with respect to parts by weight.
ール・ホルムアルデヒド樹脂(A)の25℃における不
揮発分55〜60%でのB型粘度計の粘度は6.0ps
〜15.0psであり、フェノール・ホルムアルデヒド
樹脂(B)の25℃における不揮発分50〜55%での
B型粘度計の粘度が0.5ps〜2.0psである請求
項1又は2記載の木材用接着剤。3. In order to obtain the wood adhesive, the viscosity of the phenol / formaldehyde resin (A) at 25.degree.
The wood according to claim 1 or 2, wherein the phenol-formaldehyde resin (B) has a non-volatile content of 50 to 55% at 25 ° C and a viscosity of a B-type viscometer of 0.5 to 2.0 ps. Adhesive.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29011797A JPH11124556A (en) | 1997-10-22 | 1997-10-22 | Preparation of wood adhesive |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP29011797A JPH11124556A (en) | 1997-10-22 | 1997-10-22 | Preparation of wood adhesive |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH11124556A true JPH11124556A (en) | 1999-05-11 |
Family
ID=17752030
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP29011797A Pending JPH11124556A (en) | 1997-10-22 | 1997-10-22 | Preparation of wood adhesive |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH11124556A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112646313A (en) * | 2020-12-18 | 2021-04-13 | 山东北方现代化学工业有限公司 | Thermosetting glass fiber reinforced phenolic composite material for injection and preparation method thereof |
-
1997
- 1997-10-22 JP JP29011797A patent/JPH11124556A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112646313A (en) * | 2020-12-18 | 2021-04-13 | 山东北方现代化学工业有限公司 | Thermosetting glass fiber reinforced phenolic composite material for injection and preparation method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| NZ534691A (en) | Fast curing spray-dried phenol formaldehyde resins | |
| US5637658A (en) | Modified phenol-aldehyde resin and binder system | |
| JP6043696B2 (en) | Wood board manufacturing method | |
| JPH11124555A (en) | Preparation of wood adhesive | |
| JP3594293B2 (en) | Phenolic resin adhesive composition | |
| JP2001254066A (en) | Phenol resin adhesive | |
| JP2001164228A (en) | Adhesive composition for wood | |
| US5374678A (en) | Adhesive | |
| JP2850360B2 (en) | Plywood adhesive | |
| JP2001131522A (en) | Wood adhesive composition | |
| JPH11124556A (en) | Preparation of wood adhesive | |
| JP2001152120A (en) | Adhesive composition for wood | |
| JP2001254065A (en) | Wood adhesive composition | |
| JPH11131039A (en) | Adhesive for wood | |
| JPH11172220A (en) | Wood board adhesive composition | |
| JP2004123781A (en) | Resol type phenolic resin composition, adhesive for wood materials and plywood | |
| JPH11131038A (en) | Production of adhesive for wood | |
| JP2012201728A (en) | Adhesive composition for lumber | |
| JP2001131520A (en) | Wood adhesive composition | |
| JPH11140413A (en) | Adhesive for wood | |
| JPH10259368A (en) | Adhesive for wood | |
| JP2001123141A (en) | Adhesive composition for wood | |
| JP2001131521A (en) | Wood adhesive composition | |
| JP3375059B2 (en) | Plywood molding method | |
| JPH10287859A (en) | Phenol resin adhesive |