CS257363B1 - Process for producing urea-formaldehyde condensates with specific properties - Google Patents
Process for producing urea-formaldehyde condensates with specific properties Download PDFInfo
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- CS257363B1 CS257363B1 CS866971A CS697186A CS257363B1 CS 257363 B1 CS257363 B1 CS 257363B1 CS 866971 A CS866971 A CS 866971A CS 697186 A CS697186 A CS 697186A CS 257363 B1 CS257363 B1 CS 257363B1
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Abstract
Rieši sa spůsob výroby močovinoformaldehydových kondenzátov so specifickými vlastnosťami vhodný ako lepidlo v drevárskom a nábytkárskom priemysle, ktoré sa připravuje adíciou močoviny a formaldehydu v mólovom pomere U : F 1 : 1,6 až 1: 2,2 pri pH 3,5 až 8 s výhodou 6,5 tento predkondenzát sa ďalej kontinuálně spracováva pri teplote 102 až 150 °C, tlaku 0,002 až 0,5 MPa a v druhom stupni sa dalej kondenzuje za vákua, pri teplote 40 až 80 °C za kontinuálneho přídavku vodného roztoku močoviny s prídavkom 0,01 až 5 % vápenatej soli organickej kyseliny. Množstvo močoviny do druhého stupňa odpovedá úpravě koncového mólového poměru U : F 1:1,5 až 1:1,86.The invention relates to a method for producing urea-formaldehyde condensates with specific properties suitable as adhesives in the woodworking and furniture industries, which are prepared by adding urea and formaldehyde in a molar ratio U:F 1:1.6 to 1:2.2 at a pH of 3.5 to 8, preferably 6.5. This precondensate is further continuously processed at a temperature of 102 to 150 °C, a pressure of 0.002 to 0.5 MPa and in the second stage it is further condensed under vacuum, at a temperature of 40 to 80 °C with continuous addition of an aqueous urea solution with the addition of 0.01 to 5% calcium salt of an organic acid. The amount of urea in the second stage corresponds to the adjustment of the final molar ratio U:F 1:1.5 to 1:1.86.
Description
257363257363
Vynález rieši sposob výroby močovinofor-maldehydových kondenzátov so specifický-mi vlastnosťami obsahujúce aditivum, urče-nými ako lepidlo v drevárskom a nábytkár-skom priemysle pri dýhování a ako mon-tážně lepidlo, ktoré má dobré lepiace vlast-nosti za studená za súčasnej jeho znížene]reaktivity po přidaní tužidla, pričom vply-vom aditíva dochádza zároveň k zvýšeniupevnosti.SUMMARY OF THE INVENTION The present invention provides a method for producing urea-maldehyde condensates with specific additive-containing properties to be used as a glue in the wood and furniture industry for veneering and as an assembly adhesive having good cold adhesive properties while reducing it. ] reactivity after addition of hardener, while the effect of the additive also increases in strength.
Podl'a doterajšícb postupov chráněnýchAO 209 101 sa vyrábajú močovinoformalde-hydové kondenzáty vhodné ako lepidla vdrevárskom a nábytkárskom priemysle zvodného roztoku močoviny a formaldehydudvojstupňovou polykondenzáciou, kde vprvom stupni pri teplote 102 až 150 °C, tla-ku 0,002 až 0,5 MPa v prietočnom kontinu-álnom zariadení so základným molovým po-merom vstupných surovin močoviny s for-maldehydu 1 : 1,5 až 1 : 2,2 s výhodou 1 :: 1,95 za přítomnosti 0,001 až 0,495 % hmot.,s výhodou 0,005 % hmot. organickej, aleboanorganickej kyseliny s výhodou kyselinymravčej prebehne kondenzácia. V druhomstupni sa ďalej kondenzuje pri tlaku 2 až20 kPa, pri teplote 30 až 90 °C za kontinuál-neho přídavku vodného roztoku močovinyo koncentrácii 20 až 80 % hmot., s výhodou50% hmot. a to v takom množstve, aby vý-sledný mólový poměr močoviny s formal-dehydu bol 1 : 1,3 až 1 : 1,85 a kontinuálne-ho dávkovania roztoku hydroxidov alkalic-kých kovov, alebo alkalických zemin. Ďalšie postupy přípravy podobných typovUF kondenzátov (NSR patent 2 287 921,2 444 856) chránia postupy přípravy vo vel-mi kyslom prostředí (pH výrazné pod hod-notu 5), připadne NSR pat. 2109 754 pra-cuje kontinuálně v miešaných kaskádovýchreaktorech za přítomnosti aminokyselin primeniacom sa pH od 4,2 až 8,0 za normál-ného tlaku. Z ekonomických dovodov, pokial' výrobeaUF kondenzátov je zároveň výrobcom for-maldehydu, sa vytvárajú UF kondenzáty sformaldehydu o nízkom obsahu stabilizač-ného metanolu podl'a AO 226 922 (výraznáúspora metanolu), tým sa však dosahujevysoká reaktivita UF kondenzátorov.According to the prior art processes protected by AO 209 101, urea-formaldehyde condensates suitable as adhesives are produced in the timber and furniture industry of the urea aqueous solution and formaldehyde-step polycondensation, wherein in the first stage at 102 to 150 ° C, pressures of 0.002 to 0.5 MPa in flow rate a continuous apparatus having a base molar ratio of urea feedstock to formaldehyde of 1: 1.5 to 1: 2.2, preferably 1: 1.95 in the presence of 0.001 to 0.495% by weight, preferably 0.005% by weight; . the organic or inorganic acid, preferably formic acid, is condensed. In a second stage, it is further condensed at a pressure of 2 to 20 kPa at a temperature of 30 to 90 ° C with the continuous addition of an aqueous urea solution at a concentration of 20 to 80% by weight, preferably 50% by weight. in an amount such that the resulting molar ratio of urea to formaldehyde is 1: 1.3 to 1: 1.85 and a continuous dosage of alkali metal or alkaline earth metal hydroxide solution. Other processes for the preparation of similar types of UF condensates (NSR Patent 2 287 921.2 444 856) protect the preparation processes in a very acidic environment (pH marked below 5), or NSR Pat. 2109 754 is operated continuously in stirred cascade reactors in the presence of amino acids admixing a pH of 4.2 to 8.0 under normal pressure. From the economic point of view, if the UF condensate is also a formaldehyde producer, UF condensates of formaldehyde with a low stabilizing methanol content are produced according to AO 226 922 (significant methanol savings), but the high reactivity of UF capacitors is achieved.
Pre praktické použitie je však důležité,aby výsledná živica, ktorá sa používá akopojidlo v drevárskom a nábytkárskom prie-mysle málo schopnost změny — reguláciereaktivity (hlavně zníženie) po přídavku tu-židla. Tento požiadavok vznikol rozšířenímsortimentu lepidiel pre maloodberatefov vcelej ČSSR.However, for practical use, it is important that the resulting resin, which is used as a binder in wood and furniture industry, has little ability to change - the regulation of reactivity (mainly reduction) after the addition of a solid. This requirement was created by extending the range of adhesives for small retailers in the whole of Czechoslovakia.
Podstatou tohoto vynálezu je spósob kon-tinuálnej výroby močovinoformaldehydo-vých živíc pri teplote 102 až 150 °C a tla-ku 0,002 až 0,5 MPa v prietočnom kontinu-álnom zariadení, pričom základný mólovýpoměr vstupných surovin močoviny a for-maldehydu je 1 :1,6 až 1 : 2,2 s výhodou1:1,95. Močovinoformaldehydový predkon-denzát sa připravuje predom v ©amostat- nom aparáte s formaldehydu, ktorého pHbolo upravené prídavkom hydroxidu alka-lického kovu, hydroxidu alkalických zemin,alebo sodnou sofou kyseliny boritej, alebojej derivátov s výhodou tetraboritanom sod-ným na hodnoty pH 3,5 až 8,0 s výhodou 4.5 a pevnej močoviny. Tento predkonden-zát sa dávkuje do tlakového reaktora, kdeprebieha prvý stupeň kondenzácie. V druhom reakčnom stupni prebieha ďal-šia kondenzácia přidávaného vodného roz-toku močoviny, ktorý obsahuje 0,01 až 5 %vápenatej soli organickej kyseliny s výho-dou mravčanu vápenatého. Vlastná konden-zácia prebieha pri tlaku 2 až 20 kPa a tep-lote 30 až 80 °C, pH 7 až 9 s výhodou 8,2.Komponenty sú do druhého stupňa dávko-vané kontinuálně, pričom pH sa upravujeprídavkom hydroxidov alkalických kovov,alebo alkalických zemin, alebo sodnou so-fou kyseliny boritej, alebo jej derivátov svýhodou tetraboritanom sodným. Celkovédávkované množstvo močoviny je také, abyvýsledný mólový poměr močoviny a formal-dehydu bol 1 : 5 až 1 : 1,85.SUMMARY OF THE INVENTION The subject of the present invention is a process for the continuous production of urea-formaldehyde resins at a temperature of 102 to 150 ° C and pressures of 0.002 to 0.5 MPa in a continuous continuous plant, wherein the basic molar ratio of the feedstock of urea and formaldehyde is 1: 1.6 to 1: 2.2 preferably 1: 1.95. The urea-formaldehyde preconcentrate is prepared in advance with a formaldehyde apparatus, the pH of which is adjusted by the addition of alkali metal hydroxide, alkaline earth hydroxide, or sodium boronic acid, or preferably the sodium tetraborate to pH 3.5. and 8.0, preferably 4.5, and solid urea. This precondensation is fed to a pressure reactor, where the first stage of condensation takes place. In the second reaction step, further addition of the added aqueous urea solution is carried out, which contains 0.01 to 5% of the calcium salt of the organic acid, with the exception of calcium formate. The actual condensation takes place at a pressure of 2 to 20 kPa and a temperature of 30 to 80 ° C, a pH of 7 to 9, preferably 8.2. The components are fed continuously to the second stage, the pH being adjusted by the addition of alkali metal hydroxides, or alkaline earth, or sodium boronic acid, or derivatives thereof, preferably with sodium tetraborate. The total amount of urea is such that the resulting molar ratio of urea to formaldehyde is 1: 5 to 1: 1.85.
Podfa tohoto vynálezu sa získá jednodu-chou technológiou živica s viskozitou 400až 1 800 mPa. s, ktorá je vhodná ako le-pidlo pre drevársky a nábytkářský prie-mysel, ktorá podfa obsahu retardujúcejzložky—vápenatej soli organickej kyselinymá schopnost změny reaktivity po přidanítužidla napr.: chloridu amonného.According to the invention, a simple technology provides a resin having a viscosity of 400 to 1800 mPa. s, which is suitable as a lighter for woodworking and furniture industry, which, according to the content of the retardant-calcium salt of an organic acid, has the ability to change the reactivity after addition of an amide such as ammonium chloride.
Lepidlo podfa příkladu 1 je možné použit’ako montovne lepidlo (za studená), aleboako dýhovacie lepidlo v nábytkárskom prie-mysle. Příklad 1The adhesive of Example 1 can be used as a mounting adhesive (cold) or as a veneer adhesive in the furniture industry. Example 1
Do zásobníka opatřeného miešadlom smožnosfou chladenia sa nadávkuje 15 m3vodného roztoku formaldehydu o koncen-trácii 37,1 % hmotnostných, přidá sa 20 110 %-ného vodného roztoku tetraboritanusodného na úpravu pH, ktoré je po úpravěv rozmedzi 3,5 až 7 a přidá sa 12 500 kgpevnej močoviny. Po jej rozpuštění pred-kondenzát močoviny a formaldehydu (mó-lový poměr 1 : 1,95) sa dávkuje v množstve8 až 12 m3/h do prvého reakčného stupňa,kde pri teplote 125 °C a tlaku 0,3 MPa pre-bieha kondenzačně reakcia. Produkt z pr-vého stupňa o viskozite 35 až 100 mPa. ssa kontinuálně odoberá do druhého reakč-ného stupňa, kde prebieha druhý stupeňkondenzácie prídavkom 1,3 až 1,6 m3/h50 %-ného roztoku močoviny s obsahom 1.5 % hm. mravčanu vápenatého a kontinu-álneho přídavku 10 %-ného vodného roz-toku tetraboritanu sodného tak, aby pH bo-lo v rozmedzi 7,0 až 9,0, pri teplote 60 °Ca tlaku 10,2 kPa,15 m3 of 37.1% by weight aqueous formaldehyde solution are metered into a container equipped with a stirrer for cooling, 20% of a 110% by weight aqueous tetraborate solution is added to adjust the pH, which is adjusted between 3.5 and 7 and treated with 12%. 500 kg of solid urea. After dissolving the urea-formaldehyde pre-condensate (1: 1.95 molar ratio), it is fed at a rate of 8 to 12 m 3 / h to the first reaction stage, where it is condensed at 125 ° C and 0.3 MPa pressure. reaction. The first stage product having a viscosity of 35 to 100 mPa. It is continuously withdrawn into a second reaction stage where a second stage of condensation takes place by the addition of 1.3 to 1.6 m3 / h50% urea solution containing 1.5% by weight. calcium formate and continuously adding a 10% aqueous solution of sodium tetraborate to a pH between 7.0 and 9.0 at 60 ° C and a pressure of 10.2 kPa,
Produkt z druhého reakčného stupňa sa kontinuálně odoberá, ochladzuje. Obsahuje cca 67 % hmot. UF živice, jeho viskozita jeThe product from the second reaction stage is continuously withdrawn, cooled. It contains about 67 wt. UF resin, its viscosity is
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS866971A CS257363B1 (en) | 1986-09-29 | 1986-09-29 | Process for producing urea-formaldehyde condensates with specific properties |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS866971A CS257363B1 (en) | 1986-09-29 | 1986-09-29 | Process for producing urea-formaldehyde condensates with specific properties |
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| Publication Number | Publication Date |
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| CS697186A1 CS697186A1 (en) | 1987-09-17 |
| CS257363B1 true CS257363B1 (en) | 1988-04-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CS866971A CS257363B1 (en) | 1986-09-29 | 1986-09-29 | Process for producing urea-formaldehyde condensates with specific properties |
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| CS697186A1 (en) | 1987-09-17 |
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