Summary of the invention
The technical problem that the present invention will solve provides a kind of well behaved concrete form and uses modified urea-formaldehyde resin adhesive.
Another technical problem that the present invention will solve provides the working method of the simple and clear and lower-cost concrete form of a kind of safe and reliable, easy operation, terminal point control with modified urea-formaldehyde resin adhesive.
Adopt following technical scheme for solving the problems of the technologies described above the present invention: concrete form is used modified urea-formaldehyde resin adhesive, is mainly processed by the raw material of following parts by weight: 20~30 parts in the urea of 50~60 parts in the formaldehyde of mass concentration 37%, purity 98%, 6~8 parts of trimeric cyanamides, 0.1~0.2 part of tackifier, 0.2~0.3 part of promotor.
Tackifier are Z 150PH; Promotor is vulkacit H, Dyhard RU 100 or both mixtures.
Raw material also comprises an amount of sodium hydroxide and hydrochloric acid.
Concrete form is with the working method of modified urea-formaldehyde resin adhesive, and this method may further comprise the steps:
< 1>formaldehyde and Z 150PH are dropped in the reaction kettle, agitator, the beginning heat temperature raising, temperature-stable adds mass concentration 30~36% in the time of 47~48 ℃ salt acid for adjusting pH value is 1.7~2.0;
<2>Temperature-stable added first urea equably in 7~12 minutes in the time of 51~53 ℃, it is F/U that its amount should make the mol ratio of reinforced back formaldehyde and urea
1=2.8~3.0, temperature rises to 81~85 ℃;
<3>Using the aqueous sodium hydroxide solution adjusting pH of mass concentration 25~30% immediately is 5.5~6.2, when temperature is 81~85 ℃, adds second batch of urea equably, and it is F/U that its amount should make the mol ratio of formaldehyde and urea
1+2=2.1~2.3; Stir to add after 10 minutes and account for first trimeric cyanamide of total trimeric cyanamide amount 25~40% and first promotor that accounts for total promotion dosage 1/3; Checking and adjust reactant pH is 6.8~7.2; Use muddy some method observation reactant at water form, to be white in color vaporific in 30 ℃ of water be first terminal point when reactant drips to;
< 4>reach first terminal point after, it is 7.5~8.5 that the aqueous sodium hydroxide solution that adds mass concentration 25~30% is regulated pH, adds residue trimeric cyanamide and promotor, controlled temperature stirred 20 minutes at 82 ± 1 ℃;
< 5>add residue urea, 78 ± 2 ℃ of reactions down, uses muddy some method to observe reactant at water form, to be white in color vaporific in 55~65 ℃ of water be second terminal point when reactant drips to;
< 6>reach and begin cooling behind second terminal point, when temperature was reduced to 35~45 ℃, it was 7.5~8.0 back dischargings that the aqueous sodium hydroxide solution that adds mass concentration 25~30% is regulated pH.
Contriver's abandoning tradition weak acid technology (weak base-weak acid-weak base) is used strong acid (pH 1.7~2.0) technology (strong acid-weak acid-weak base) glue instead.To reactant under the strong acid condition to mole highstrung characteristics of the residence time when; The custom that discarded common urea feeds intake fast; The working method that proposition evenly added in 7~12 minutes; The gelling phenomenon appears to avoid the too fast local molar ratio that causes of urea adding low excessively, can not cross causing overstand slowly.Temperature, pH value, feed rate, reinforced time and mol ratio that the strong acid stage must grasp are proposed simultaneously; According to these concrete operations step and precise information; Need not to add stopper and also need not hang down temperature control; Also can control reaction safely and reliably, obtain to improve the urea-formaldehyde resin (containing the Uron ring) of structure.Certainly reaction kettle varies in size, and feeding quantity and reinforced time also need corresponding adjustment, but finally with the temperature that adds material at 81~85 ℃ and do not produce the gelling phenomenon and be as the criterion.Then, under weak acid-weak base condition,, can strengthen the physical and mechanical property of urea-formaldehyde resin adhesive again, thereby use modified urea-formaldehyde resin adhesive with the preferable concrete form of less trimeric cyanamide obtained performance with cyanurotriamide modified, specifically:
After first urea feeds intake and finishes, add alkali immediately and make the reactant disengaging strong acid stage and get into weak acid stage.Still exist a large amount of free formaldehydes in the reaction mass this moment.Thereby must add second batch of urea, and the mol ratio of control formaldehyde and urea is to guarantee resin quality.Because the existing water-fast effect that improves intensity that has again of trimeric cyanamide makes it at weak acid and near participating in reaction under the neutrallty condition so drop into trimeric cyanamide, generate cyanurotriamide modified urea-formaldehyde resin (MUF) simultaneously.After first terminal point arrives, add alkali and make reactant get into the weak base stage, and add second batch of trimeric cyanamide, add the 3rd batch of urea again behind the stirring certain hour, they are reacted under the weak base condition, thereby play the effect of urea-formaldehyde resin being carried out further modification.
In addition, working method of the present invention has two simple and clear, maneuverable terminal point controlling index (promptly splash into reactant respectively white cloud and mist whether to occur in 30 ℃ and 55~65 ℃ of water be sign), with the convenient process of controlling.
Embodiment
Embodiment 1
1, prescription is formed
The mol ratio of formaldehyde and urea is F/U=2.04,530 parts in formaldehyde (concentration 37%), 197 parts in urea (purity 98%), 65 parts of trimeric cyanamides, 1.4 parts of Z 150PH, 1 part of vulkacit H, 2 parts of Dyhard RU 100s.
2, adhesive-preparing technology
< 1>with in 530 parts of formalins and 1.4 parts of input reaction kettles of Z 150PH, agitator, the beginning heat temperature raising stops heating when being warmed up to 38~40 ℃, and when temperature inertia increased to 48 ℃, the salt acid for adjusting pH value of use 31~36% was 1.7~2.0;
When < 2>temperature increases to 51 ℃, evenly add 140 parts in first urea in 7~10 minutes, temperature is raised to 83~85 ℃;
< 3>using 25~30% aqueous sodium hydroxide solutions to regulate pH immediately is 5.8~6.2;, temperature adds 35 parts in second batch of urea when being 83~85 ℃ equably; Stir after 10 minutes and to add 25 parts of trimeric cyanamides and 1 part of vulkacit H, checking and adjust reactant pH is 6.8~7.2, uses muddy some method to observe; Reactant is splashed in 30 ℃ of water, and the cloud that is white in color is first terminal point;
< 4>reach first terminal point after, adding 25~30% aqueous sodium hydroxide solutions, to regulate pH be 7.5~8.5, adds 2 parts of 40 parts of trimeric cyanamides and Dyhard RU 100s, temperature is controlled at 82 ± 1 ℃, stirs 20 minutes;
< 5>add 22 parts in the 3rd batch of urea, be allowed to condition at and carry out polycondensation (reactant is splashed in 55~65 ℃ of water, and the cloud that is white in color is second terminal point) under 78 ± 2 ℃;
< 6>reach and begin cooling behind second terminal point, when temperature was reduced to 35~45 ℃, adding 25~30% aqueous sodium hydroxide solution, to regulate pH be 7.5~8.0 back dischargings.
3, the quality of glue (seeing table 1)
The quality condition of table 1 embodiment 1 glue
4, making sheet effect
< 1>mask-making technology significant parameter
Nine layers of Eucalyptus veneer, the thick 1.5~1.8mm of veneer, water ratio≤14%, tackiness agent add 10% wheat-flour, do not add solidifying agent, resin added 200~250g/m
2
Hot pressing temperature=105~110 ℃, hot pressing time=1.2~1.5min/mm.
< 2>concrete form quality (thickness of slab 15mm sees table 2)
The quality condition of table 2 embodiment 1 concrete form
Embodiment 2
1, prescription is formed
The mol ratio of formaldehyde and urea is F/U=1.82,590 parts in formaldehyde (concentration 37%), 245 parts in urea (purity 98%), 75 parts of trimeric cyanamides, 1.5 parts of Z 150PH, 1 part of vulkacit H, 2 parts of Dyhard RU 100s;
2, adhesive-preparing technology
< 1>with in 590 parts of formalins and 1.5 parts of input reaction kettles of Z 150PH, agitator, the beginning heat temperature raising stops heating when being warmed up to 38~40 ℃, and when temperature inertia increased to 48 ℃, the salt acid for adjusting pH value of use 31~36% was 1.7~2.0;
When < 2>temperature increases to 51 ℃, evenly add 156 parts in first urea in 7~10 minutes, temperature is raised to 81~85 ℃.
< 3>using 25~30% aqueous sodium hydroxide solutions to regulate pH immediately is 5.5~6.0;, temperature adds 38 parts in second batch of urea when being 83~85 ℃ equably; Stir after 10 minutes and to add 30 parts of trimeric cyanamides and 1 part of vulkacit H, checking and adjust reactant pH is 6.8~7.2, uses muddy some method to observe; Reactant is splashed in 30 ℃ of water, and the cloud that is white in color is first terminal point;
< 4>reach first terminal point after, adding 25~30% aqueous sodium hydroxide solutions, to regulate pH be 7.5~8.5, adds 2 parts of 45 parts of trimeric cyanamides and Dyhard RU 100s, temperature is controlled at 82 ± 1 ℃, stirs 20 minutes;
< 5>add 51 parts in the 3rd batch of urea, be allowed to condition at and carry out polycondensation under 78 ± 2 ℃ (reactant is splashed in 55~65 ℃ of water, and the cloud and mist that is white in color is second terminal point;
< 6>reach and begin cooling behind second terminal point, when temperature was reduced to 35~45 ℃, adding 25~30% aqueous sodium hydroxide solution, to regulate pH be 7.5~8.0 back dischargings.
3, the quality of glue (seeing table 3)
The quality condition of table 3 embodiment 2 glue
4, making sheet effect
< 1>mask-making technology significant parameter
Nine layers of Eucalyptus veneer, the thick 1.5~1.8mm of veneer, water ratio≤14%, tackiness agent add 10% wheat-flour, do not add solidifying agent, resin added 200~250g/m
2
Hot pressing temperature=105~110 ℃, hot pressing time=1.2~1.5min/mm.
< 2>concrete form quality (thickness of slab 15mm sees table 4)
The quality condition of table 4 embodiment 2 concrete forms
Embodiment 3
1, prescription is formed
The mol ratio of formaldehyde and urea is F/U=2.107,1200 parts in formaldehyde (concentration 37%), 430 parts in urea (purity 98%), 115 parts of trimeric cyanamides, 3 parts of Z 150PH, 2 parts of vulkacit Hs, 4 parts of Dyhard RU 100s;
2, adhesive-preparing technology
< 1>with in 1200 parts of formalins and 3 parts of input reaction kettles of Z 150PH, agitator, the beginning heat temperature raising stops heating when being warmed up to 37~38 ℃, and when temperature inertia increased to 47 ℃, the salt acid for adjusting pH value of use 30~36% was 1.7~2.0;
When < 2>temperature increases to 51 ℃, evenly add 312 parts in first urea in 10~12 minutes, temperature is raised to 83~85 ℃.
< 3>using 25~30% aqueous sodium hydroxide solutions to regulate pH immediately is 5.5~6.0;, temperature adds 76 parts in second batch of urea when being 83~85 ℃ equably; Stir after 10 minutes and to add 40 parts of trimeric cyanamides and 2 parts of vulkacit Hs, checking and adjust reactant pH is 6.8~7.2, uses muddy some method to observe; Reactant is splashed in 30 ℃ of water, and the cloud that is white in color is first terminal point;
< 4>reach first terminal point after, adding 25~30% aqueous sodium hydroxide solutions, to regulate pH be 7.5~8.5, adds 4 parts of 75 parts of trimeric cyanamides and Dyhard RU 100s, temperature is controlled at 82 ± 1 ℃, stirs 20 minutes;
< 5>add 42 parts in the 3rd batch of urea, be allowed to condition at and carry out polycondensation under 78 ± 2 ℃ (reactant is splashed in 55~65 ℃ of water, and the cloud and mist that is white in color is second terminal point;
< 6>reach and begin cooling behind second terminal point, when temperature was reduced to 35~45 ℃, adding 25~30% aqueous sodium hydroxide solution, to regulate pH be 7.5~8.0 back dischargings.
3, the quality of glue (seeing table 5)
The quality condition of table 5 embodiment 3 glue
4, making sheet effect
< 1>mask-making technology significant parameter
Nine layers of Eucalyptus veneer, the thick 1.5~1.8mm of veneer, water ratio≤14%, tackiness agent add 10% wheat-flour, do not add solidifying agent, resin added 200~250g/m
2
Hot pressing temperature=105~110 ℃, hot pressing time=1.2~1.5min/mm.
< 2>concrete form quality (thickness of slab 15mm sees table 6)
The quality condition of table 6 embodiment 3 concrete forms