CN1115369C - Process for preparing adhesive of urea-formaldehyde resin - Google Patents

Process for preparing adhesive of urea-formaldehyde resin Download PDF

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Publication number
CN1115369C
CN1115369C CN 98110988 CN98110988A CN1115369C CN 1115369 C CN1115369 C CN 1115369C CN 98110988 CN98110988 CN 98110988 CN 98110988 A CN98110988 A CN 98110988A CN 1115369 C CN1115369 C CN 1115369C
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China
Prior art keywords
urea
reaction
sodium hydroxide
reactor
formaldehyde resin
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Expired - Fee Related
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CN 98110988
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Chinese (zh)
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CN1243854A (en
Inventor
陈剑慧
许志钢
管晨
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YANGGUANG CULTURAL ARTICLES CO Ltd HANGZHOU CITY
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YANGGUANG CULTURAL ARTICLES CO Ltd HANGZHOU CITY
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Priority to CN 98110988 priority Critical patent/CN1115369C/en
Publication of CN1243854A publication Critical patent/CN1243854A/en
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Publication of CN1115369C publication Critical patent/CN1115369C/en
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  • Phenolic Resins Or Amino Resins (AREA)
  • Adhesives Or Adhesive Processes (AREA)

Abstract

The present invention discloses a preparation method for urea-formaldehyde resin adhesive, which comprises: the molar ratio of urea to formaldehyde is controlled between 1:1.2 and 2.0; the water solution of sodium hydroxide, triethanolmine and hexamethylenetetramine is adopted as a catalyst, and the urea is added at different times, wherein a fine flow dropping method is adopted for adding urea for the first time; reaction is carried out under the condition of weak acidity. The reaction speed of the present invention is rapid. Generated resin adhesive has the advantages of high bonding strength, favorable appearance and favorable stability; meanwhile, a polysiloxane surfactant is added into liquid state urea-formaldehyde resin in the present invention. A product has excellent anticaking performance, and can be widely applied to the processing industry of bamboo, wood, fodder, etc.

Description

A kind of Preparation of urea-formaldehyde resin adhesive method
The present invention relates to a kind of preparation method of aminoresin tackiness agent.
Urea formaldehyde resin adhesive is with low cost because of its raw material is easy to get at present, already is extensive use of at the bamboo lumber yard, has also obtained application simultaneously in granulated meal processing.The urea-formaldehyde resin adhesive production technique comprises the urea of certain mol proportion and formaldehyde under catalyst action, carries out addition reaction and polycondensation.The addition reaction of urea and formaldehyde is carried out under weak basic condition usually, and the polycondensation of urea and formaldehyde is carried out under solutions of weak acidity usually, discloses this technology as Chinese patent CN1038100C.But adopt this technology, speed of response is slow, and the bond properties of resin, outward appearance and stability can not be satisfactory.
The object of the present invention is to provide a kind of degree of adhesion height, have the Preparation of urea-formaldehyde resin adhesive method of good appearance and stable performance.
For achieving the above object, the present invention by the following technical solutions: the mol ratio of urea and formaldehyde is controlled at 1: between the 1.2-2.0, these two kinds of raw materials are in and carry out addition and polycondensation under the solutions of weak acidity, and comprise the steps:
A), formalin is added in the reactor, start stirring, and the adding basic catalyst is regulated pH value=5.5-7.0, described basic catalyst is the aqueous solution of sodium hydroxide, trolamine, hexamethylenetetramine, its weight proportion is a sodium hydroxide: three ethanol: six methynes, four ammonia: water=1-3: 0.5-20: 0.2-10: 100-200, and be warming up to 65-85 ℃;
B), the logical steam of the 55-85% of required urea total amount is melted, temperature is controlled at 75-85 ℃, and thread splashes into reactor in 20-40 minute;
C), drip urea after, between 90-100 ℃ insulation reaction 30-60 minute;
D), the usefulness 5-10% ammonia chloride aqueous solution is regulated pH value=4-5.5, and is added the surplus urea reaction to terminal;
E), with the pH value=6.5-7.5 of 10-15% aqueous sodium hydroxide solution conditioned reaction liquid, termination reaction;
F), use the chuck water quench to 30-45 ℃ of discharging barrelling reactor.
The present invention also can adopt following further technical scheme: add the polysiloxane surfactant of 0.1-1.0% at the reactant of discharging, carry out spraying drying then.
In general, being reflected under the solutions of weak acidity of urea and formaldehyde carried out, speed of response is very fast, Resin adhesive bond strength height, the outward appearance that generates and having good stability, though thermal discharge is big in its reaction process, in the production as control improper easy generation gelatin phenomenon, but owing to adopted technique scheme, splash into reactor after particularly the logical steam of urea being melted, and the selection by temperature of reaction, time, pH value, make that the speed of response of urea and formaldehyde is controlled effectively, broken through the forbidden zone that urea-formaldehyde resin in the past prepares under solutions of weak acidity; Can make the urea-formaldehyde resin prevented from caking owing in the reactant of discharging, add polysiloxane surfactant simultaneously, be in Powdered uniformly, easy to use.
The invention will be further described below in conjunction with embodiment.
Embodiment 1:
The mol ratio of urea and formaldehyde is 1: 1.6, and its reaction process step is as follows:
A), 37% formalin with 350kg adds in the reactor, and the adding basic catalyst is regulated pH value=6.5 under constantly stirring, described basic catalyst is the aqueous solution of sodium hydroxide, trolamine, hexamethylenetetramine, its weight proportion is a sodium hydroxide: trolamine: hexamethylenetetramine: water=1.2: 0.9: 0.7: 1 20, and be warming up to 68 ℃
B), be that the logical steam of 125kg melts with 78% of required urea total amount, temperature is controlled at 80 ℃, and thread splashes into reactor in 25 minutes,
C), drip urea after, 92 ℃ of insulation reaction 35 minutes,
D), with 10% ammonia chloride aqueous solution conditioned reaction liquid pH value=4.8, and add 35 remaining kg urea reactions to 20 ℃ of cloud points,
E), with pH value=7.0 of 15% aqueous sodium hydroxide solution conditioned reaction liquid, termination reaction,
F), with logical chuck cooling water temperature to the 35 ℃ discharging of reactor.
G), add the polysiloxane surfactant that accounts for reactant weight 0.25%, carry out spraying drying then and make powdery product at the reactant of discharging.
Embodiment 2:
The mol ratio of urea and formaldehyde is 1: 1.25, and its reaction process step is as follows:
A), 37% formalin with 380kg adds in the reactor, and the adding basic catalyst is regulated pH value=6.0 under constantly stirring, described basic catalyst is the aqueous solution of sodium hydroxide, trolamine, hexamethylenetetramine, its weight proportion is a sodium hydroxide: trolamine: hexamethylenetetramine: water=1.8: 2.1: 1.5: 150, and be warming up to 75 ℃
B), be that the logical steam of 160kg melts with 70% of required urea total amount, temperature is controlled at 80 ℃, and thread splashes into reactor in 35 minutes,
C), drip urea after, 95 ℃ of insulation reaction 52 minutes,
D), with 10% ammonia chloride aqueous solution conditioned reaction liquid pH value=5.3, and add remaining 70kg urea reaction to 20 ℃ of cloud points,
E), with pH value=7.0 of 15% aqueous sodium hydroxide solution conditioned reaction liquid, termination reaction,
F), with logical chuck cooling water temperature to the 30 ℃ discharging of reactor.
G), add the polysiloxane surfactant that accounts for reactant weight 0.55%, carry out spraying drying then and make powdery product at the reactant of discharging.
Embodiment 3:
The mol ratio of urea and formaldehyde is 1: 1.85, and its reaction process step is as follows:
A), 37% formalin with 420kg adds in the reactor, and the adding basic catalyst is regulated pH value=5.8 under constantly stirring, described basic catalyst is the aqueous solution of sodium hydroxide, trolamine, hexamethylenetetramine, its weight proportion is a sodium hydroxide: trolamine: hexamethylenetetramine: water=2.5: 6.0: 3.5: 180, and be warming up to 68 ℃
B), be that the logical steam of 111kg melts with 65% of required urea total amount, temperature is controlled at 82 ℃, and thread splashes into reactor in 28 minutes,
C), drip urea after, 98 ℃ of insulation reaction 45 minutes,
D), with 10% ammonia chloride aqueous solution conditioned reaction liquid pH value=4.5, and add remaining 60kg urea reaction to 20 ℃ of cloud points,
E), with pH value=7.0 of 15% aqueous sodium hydroxide solution conditioned reaction liquid, termination reaction,
F), with logical chuck cooling water temperature to the 30 ℃ discharging of reactor.
G), add the polysiloxane surfactant that accounts for reactant weight 0.85%, carry out spraying drying again and make powdery product at the reactant of discharging.

Claims (2)

1, a kind of Preparation of urea-formaldehyde resin adhesive method, the mol ratio of urea and formaldehyde is controlled at 1: between the 1.2-2.0, it is characterized in that these two kinds of raw materials are under the solutions of weak acidity reacts, and comprises the steps:
A), formalin is added in the reactor, start stirring, and the adding basic catalyst is regulated pH value=5.5-7.0, described basic catalyst is the aqueous solution of sodium hydroxide, trolamine, hexamethylenetetramine, its weight proportion is a sodium hydroxide: trolamine: six methynes, four ammonia: water=1-3: 0.5-20: 0.2-10: 100-200, and be warming up to 65-85 ℃;
B), the logical steam of the 55-85% of required urea total amount is melted, temperature is controlled at 75-85 ℃, and thread splashes into reactor in 20-40 minute;
C), drip urea after, between 90-100 ℃ insulation reaction 30-60 minute;
D), the usefulness 5-10% ammonia chloride aqueous solution is regulated pH value=4-5.5, and is added the surplus urea reaction to terminal;
E), with the pH value=6.5-7.5 of 10-15% aqueous sodium hydroxide solution conditioned reaction liquid, termination reaction;
F), reactor is led to the chuck cooling water temperature to 30-45 ℃ of discharging barrelling.
2, a kind of Preparation of urea-formaldehyde resin adhesive method as claimed in claim 1 is characterized in that the polysiloxane surfactant at the reactant adding 0.1-1.0% of discharging, then spraying drying.
CN 98110988 1998-07-31 1998-07-31 Process for preparing adhesive of urea-formaldehyde resin Expired - Fee Related CN1115369C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 98110988 CN1115369C (en) 1998-07-31 1998-07-31 Process for preparing adhesive of urea-formaldehyde resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 98110988 CN1115369C (en) 1998-07-31 1998-07-31 Process for preparing adhesive of urea-formaldehyde resin

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CN1243854A CN1243854A (en) 2000-02-09
CN1115369C true CN1115369C (en) 2003-07-23

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100384899C (en) * 2006-03-15 2008-04-30 北京林业大学 Urea resin and production thereof

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102250572B (en) * 2011-06-17 2013-06-05 江苏赛奥生化有限公司 Preparation method of oxidized pueraria starch adhesive
CN103192441B (en) * 2013-04-19 2015-07-22 琚长林 Plant fiber composite fireproof plate
CN103834338A (en) * 2014-03-20 2014-06-04 浙江红高梁木业有限公司 Adhesive for artificial board and preparation method thereof
CN103936524B (en) * 2014-05-08 2016-04-27 河南力浮科技有限公司 A kind of production method of urea aldehyde slow-release compound fertilizer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100384899C (en) * 2006-03-15 2008-04-30 北京林业大学 Urea resin and production thereof

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