Patent Description:
Low application viscosity of polyurethane reactive hotmelt (PU RHM) is desired for fast and easy application process in adhesives area and additive manufacturing (3D printing), but the disadvantage is that it takes time to build up sufficient strength for further handling steps. Therefore, the challenge is to develop a PU RHM system with low viscosity, short setting time and in the mean time having fast green strength building-up properties.

<CIT> discloses a method for preparing an optical/wet dual-curable polyurethane hotmelt, which comprises a very complex three-steps synthesis. In addition, HDI trimer is used, which may lead to high viscosity of the hotmelt and the low impact strength of the cured product.

<CIT> discloses a polymerizable liquid useful for the production of a three-dimensional object comprised of polyurethane, polyurea, or a copolymer thereof by additive manufacturing, said polymerizable liquid comprising a mixture of: (i) a blocked or reactive blocked prepolymer, (ii) a blocked or reactive blocked diisocyanate, or (iii) a blocked or reactive blocked diisocyanate chain extender. However, A very complexed <NUM> component system is used in <CIT> which requires multi step of chemistry synthesis of the blocked diisocyanate or prepolymer; a special complicated design of the 3D printing machine; the dead layer in <CIT> is wasting materials; toughness of the printed objects is not so good.

Disclosed is a polyurethane so that an UV-moisture dual cure polyurethane reactive hotmelt with low viscosity, short setting time and in the mean time having fast green strength building-up properties could be obtained by using said polyurethane.

Disclosed is a process for preparing the polyurethane.

A further object of the present invention is to provide an UV-moisture dual cure polyurethane reactive hotmelt comprising the polyurethane of the present invention.

A further object of the present invention is to provide a method for manufacturing a three-dimensional object by using the UV-moisture dual cure polyurethane reactive hotmelt as well as the three-dimensional object with high toughness obtainable by said method.

One aspect of the present disclosure is directed to a polyurethane which has an isocyanate group and has C-C double bonds on the side chain, wherein the isocyanate in the isocyanate component for synthesizing the polyurethane is diisocyanate and the isocyanate component comprises at least one diisocyanate having C-C double bonds on the side chain.

The undefined article "a", "an", "the" means one or more of the species designated by the term following said article.

The amount of the C-C double bond is <NUM> to <NUM> mol/kg, for example <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM> mol/kg, pereferably, <NUM> to <NUM> mol/kg, based on the total weight of the polyurethane.

The content of isocyanate group can be in the range from <NUM> to <NUM>% by weight, for exampl <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>% by weight, preferably <NUM> to <NUM>% by weight, based on the total weight of the polyurthane.

According to one imbodiment, the polyurethane is obtained from the reaction of an isocyanate component with a polyol component, and wherein the isocyanate component comprises at least one diisocyanate having C-C double bonds on the side chain.

According to one preferred embodiment, the average number of C-C double bond in the diisocyanate having C-C double bonds on the side chain is <NUM> to <NUM> per molecule, for example <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM> per molecule or about <NUM> per molecule, pereferably <NUM> to <NUM> per molecule, for example <NUM> to <NUM> per molecule.

The amount of the diisocyanate having C-C double bond on the side chain can be in the range from <NUM> to <NUM>% by weight, for example <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>% by weight, preferably <NUM> to <NUM>% by weight, based on the total weight of the isocyanate component and the polyol component.

In one preferred embodiment, the isocyanate component can comprise at least one further isocyanate and said further isocyanate is diisocyanate. The further diisocyanate can adjust the UV reactivity of the hotmelt. The further diisocyanate can be selected from aliphatic, aromatic and cycloaliphatic diisocyanates. Examples of aromatic diisocyanates are <NUM>,<NUM>-tolylene diisocyanate (<NUM>,<NUM>-TDI), <NUM>,<NUM>'-diphenylmethane diisocyanate (<NUM>,<NUM>'-MDI), <NUM>,<NUM>'-diphenylmethane diisocyanate (<NUM>,<NUM>'-MDI), <NUM>,<NUM>'-diphenylmethane diisocyanate (<NUM>,<NUM>'-MDI) and so-called TDI mixtures (mixtures of <NUM>,<NUM>-tolylene diisocyanate and <NUM>,<NUM>-tolylene diisocyanate).

Examples of aliphatic diisocyanates are <NUM>,<NUM>-butylene diisocyanate, <NUM>,<NUM>-dodecamethylene diisocyanate, <NUM>,<NUM>-decamethylene diisocyanate, <NUM>-butyl-<NUM>-ethylpenta-methylene diisocyanate, <NUM>,<NUM>,<NUM>-trimethylhexamethylene diisocyanate or <NUM>,<NUM>,<NUM>-trimethylhexamethylene diisocyanate and in particular hexamethylene diisocyanate (HDI).

Examples of cycloaliphatic diisocyanates are isophorone diisocyanate (IPDI), <NUM>-isocyanatopropylcyclohexyl isocyanate, <NUM>,<NUM>'-methylenebis(cyclohexyl) diisocyanate and <NUM>-methylcyclohexane <NUM>,<NUM>-diisocyanate (H-TDI).

Further examples of isocyanates having groups of differing reactivity are <NUM>,<NUM>-phenylene diisocyanate, <NUM>,<NUM>-phenylene diisocyanate, <NUM>,<NUM>-naphthylene diisocyanate, diphenyl diisocyanate, tolidine diisocyanate and <NUM>,<NUM>-tolylene diisocyanate.

The amount of the further diisocyanate can be in the range from <NUM> to <NUM>% by wight, for example <NUM> to <NUM> or <NUM> to <NUM> or <NUM> to <NUM>% by weight, preferably <NUM> to <NUM>% by weight, based on the total weight of the isocyanate component and the polyol component.

According to one preferred embodiment, the polyol component comprises at leat one crystalline polyester polyol and/or at least one non-crystalline polyester polyol.

The non-crystalline polyester polyols have no melting point and have a glass transition temperature (Tg) of at least -<NUM>. The crystalline Polyester polyols have a melting point, the melting point being preferably at least <NUM>, more preferably at least <NUM>.

The glass transition temperature and the melting point can be measured according to DIN <NUM>.

Crystalline polyester polyol can be prepared from the reaction of one or more linear aliphatic dicarboxylic acids with at least <NUM> carbon atoms, preferably at least <NUM> carbon atoms, particularly preferably <NUM> to <NUM> carbon atoms, such as adipic acid, azelaic acid, sebacic acid or dodecanedioic acid, with one or more linear diols having at least <NUM> carbon atoms at least <NUM> carbon atoms, more preferably <NUM> to <NUM> carbon atoms, <NUM>,<NUM>-butanediol and <NUM>,<NUM>-hexanediol. Also suitable are polycaprolactone.

The molecule weight of the crystalline polyester polyol can be in the range from <NUM> to <NUM>/mol, preferably <NUM> to <NUM>/mol.

Accroding to one embodiment, the crystalline polyester polyol has a hydroxyl number in the range from15 to <NUM> KOH/g, preferably from <NUM> to <NUM> KOH/g.

The amount of crystalline polyester polyol can be in the range from <NUM> to <NUM>% by weight, for example <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>% by weight, preferably <NUM> to <NUM>% by weight, based on the total weight of the isocyanate component and the polyol component.

Non-crystalline polyester polyols can be prepared from the reaction of one or more carboxylic acid components selected from adipic acid, isophthalic acid and terephthalic acid with one or more alcohol components selected from ethylene glycol, diethylene glycol, propylene glycol and neopentyl glycol.

The molecule weight of the non-crystalline polyester polyol can be in the range from <NUM> to <NUM>/mol, preferably <NUM> to <NUM>/mol.

Accroding to one embodiment, the non-crystalline polyester polyol has a hydroxyl number in the range from10 to <NUM> KOH/g, preferably <NUM> to <NUM> KOH/g.

The amount of non-crystalline polyester polyol can be in the range from <NUM> to <NUM>% by weight, for example <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>% by weight, preferably <NUM> to <NUM>% by weight, based on the total weight of the isocyanate component and the polyol component.

In one embodiment, the polyol component comprises at least one crystalline polyether polyol. The crystalline polyether polyol has a melting point, the melting point being preferably at least <NUM>, more preferably at least <NUM>.

The crystalline polyether polyol comprises, for example poly(oxypropylene) polyol and polytetrahydrofuran.

The molecule weight of the crystalline polyether polyol can be in the range from <NUM> to <NUM>/mol, preferably <NUM> to <NUM>/mol.

Accroding to one embodiment, the crystalline polyether polyol has a hydroxyl number in the range from <NUM> to <NUM> KOH/g, preferably <NUM> to <NUM> KOH/g.

The amount of crystalline polyether polyol can be in the range from <NUM> to <NUM>% by weight, for example <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>, <NUM> to <NUM>% by weight, preferably from <NUM> to <NUM>% by weight, based on the total weight of the isocyanate component and the polyol component.

In one embodiment, the polyol component comprise at least one non-crystalline polyehter polyol. The non-crystalline polyether polyol has no melting point and have a glass transition temperature of at least -<NUM>.

Preferred non-crystalline polyether glycol(s) comprise one or more linear diol(s) in which the hydroxyl groups are separated by repeating tetramethylene and <NUM>-methyl tetramethylene ether groups.

Examples of such glycols are a liquid (at room temperature) copolymers of tetrahydrofuran (THF ) and <NUM>-methyl-THF of the following structure:
<CHM>
m+n=integer from <NUM> to <NUM>; Mw about <NUM>,<NUM>; OHav about <NUM>; Tg -<NUM>.

The molecule weight of the non-crystalline polyether polyol can be in the range from <NUM> to <NUM>/mol, preferably <NUM> to <NUM>/mol.

Accroding to one embodiment, the non-crystalline polyether polyol has a hydroxyl number in the range from30 to <NUM> KOH/g, preferably <NUM> to <NUM> KOH/g.

The amount of non-crystalline polyether polyol can be in the range from <NUM> to <NUM>% by weight, for example <NUM> to <NUM>% by weight, based on the total weight of the isocyanate component and the polyol component.

In a pereferred embodiment, the polyurethane according to the present invention is obtained from the reaction of an isocyanate component with a polyol component, wherein isocyanate component comprises:.

Wherein the weight % is based on total weight of the isocyanate component and the polyol component.

In another pereferred embodiment, the polyurethane according to the present invention is obtained from the reaction of an isocyanate component with a polyol component, wherein isocyanate component comprises:.

wherein the weight % is based on total weight of the isocyanate component and the polyol component.

Usually, the polyols used in the polyol component, for example crystalline polyester polyol, non-crystalline polyester polyol, crystalline polyether polyol and non-crystalline polyether polyol have a functionality of <NUM>.

Another aspect of the present invention is directed to a method for preparing the polyurethane of the present invention, which comprises reacting the isocyanate component with the polyol component to obtain the polyurethane having an isocyanate group and having C-C double bonds on the side chain, wherein the isocyanate component comprises at least one diisocyanate having C-C double bonds on the side chain.

In one preferred embodiment, the polyol component can be heated to melt all polyols. Then, isocyanate component is added to carry out the reaction. The reaction temperature can be in the range from <NUM> to <NUM>, preferably from <NUM> to <NUM>.

A further aspect of the present invention is directed to an UV-moisture dual cure polyurethane reactive hotmelt, which comprises at least one polyurethane of the present invention.

According to one preferred embodiment, the UV-moisture dual cure polyurethane reactive hotmelt further comprises at least one photoinitiator.

Suitable photoinitiators include for example those which do not degrade under the application temperature of the UV-moisture dual cure polyurethane reactive hotmelt. Examples of the photoinitiator include an acylphosphine oxide compound, a benzophenone compound, an acetophenone compound, an oxime ester compound, a benzoin compound, especially a benzoin ether compound, thioxanthone, and the like. According to a preferred embodiment, the photointiator is <NUM>,<NUM>,<NUM>-trimethylbenzoyldiphenylphosphine oxide.

The amount of photoinitiator can be in the range from <NUM> to <NUM>% by weight, preferably <NUM> to <NUM>% by weight, based on the total weight of the PU reactive hotmelt.

According to a preferred embodiment, the UV-moisture dual cure polyurethane reactive hotmelt of the present invention can have a Brookfield viscosity of less than <NUM> Pas, for example less than <NUM> Pas or less than <NUM> Pas measured at <NUM>.

According to another preferred embodiment, the UV-moisture dual cure polyurethane reactive hotmelt of the present invention can have a Brookfield viscosity of less than <NUM> Pas, for example less than <NUM> Pas or less than <NUM> Pas or less than <NUM> Pas measured at <NUM>.

In one embodiment, the UV-moisture dual cure polyurethane reactive hotmelt of the present invention can comprise at least one urea reaction catalyst to promote the reaction of isocyanate group with moisture.

Useful catalysts include for example all catalysts typically used in polyurethane chemistry.

Catalysts typically used in polyurethane chemistry are preferably organic amines, especially tertiary aliphatic, cycloaliphatic or aromatic amines.

As customary organic amines there may be mentioned by way of example: triethylamine, <NUM>,<NUM>-diazabicyclo[<NUM>,<NUM>,<NUM>]octane, tributylamine, dimethylbenzylamine, N,N,N',N'-tetramethylethylenediamine, N,N,N',N'-tetramethylbutane-<NUM>,<NUM>-diamine, N,N,N',N'-tetramethylhexane-<NUM>,<NUM>-diamine, dimethylcyclohexylamine, dimethyldodecylamine, pentamethyldipropylenetriamine, pentamethyldiethylenetriamine, <NUM>-methyl-<NUM>-dimethylamino-<NUM>-azapentol, dimethylaminopropylamine, <NUM>,<NUM>-bisdimethylaminobutane, bis(<NUM>-dimethylaminoethyl) ether, N-ethylmorpholine, N-methylmorpholine, N-cyclohexylmorpholine, <NUM>-dimethylaminoethoxyethanol, dimethylethanolamine, tetra-methylhexamethylenediamine, dimethylamino-N-methylethanolamine, N-methylimidazole, N-formyl-N,N'-dimethylbutylenediamine, N-dimethylaminoethyl- morpholine, <NUM>,<NUM>'-bisdimethylamino-di-n-propylamine and/or <NUM>,<NUM>'-dipiparazine diisopropyl ether, dimethylpiparazine, tris(N,N-dimethylaminopropyl)-s-hexahydrotriazine, imidazoles such as <NUM>,<NUM>-dimethylimidazole, <NUM>-chloro-<NUM>,<NUM>-dimethyl-<NUM>-(N-methylaminoethyl)imidazole, <NUM>-aminopropyl-<NUM>,<NUM>-dimethoxy-<NUM>-methylimidazole, <NUM>-aminopropyl-<NUM>,<NUM>,<NUM>-tributylimidazole, <NUM>-aminoethyl-<NUM>-hexylimidazole, <NUM>-aminobutyl-<NUM>,<NUM>-dimethylimidazole, <NUM>-(<NUM>-aminopropyl)-<NUM>-ethyl-<NUM>-methylimidazole, <NUM>-(<NUM>-aminopropyl)imidazole, <NUM>-(<NUM>-aminopropyl)-<NUM>-methylimidazole, and/or <NUM>,<NUM>'-dimorpholinodiethylether.

It will be appreciated that mixtures of two or more of the aforementioned compounds may be used as urea reaction catalysts as well.

The amount of urea reaction catalyst can be in the range from <NUM> to <NUM>% by weight or <NUM> to <NUM>% by weight, based on the total weight of the hotmelt.

The hotmelt of the present invention preferably comprises at least one further additive selected from tackifiers, stabilizers, fillers, flow control agents, thickeners, wetting agents, defoamers, crosslinkers, plasticizers, ageing inhibitors, fungicides, pigments, dyes, matting agents, and neutralizing agents. The hotmelt preferably comprises from <NUM> to <NUM>% by weight of one or more polyurethane of the invention as described herein and at least <NUM>% by weight of one or more tackifiers, based on the total amount of the hotmelt.

Tackifiers are known per se to the skilled person. They are additives for adhesives or elastomers that improve the autoadhesion (tack, intrinsic stickiness, self-adhesion) of these systems. They generally have a relatively low molar mass (Mn about <NUM>-<NUM>/mol), a glass transition temperature which lies above that of the elastomers. The amount by weight of the tackifiers is preferably <NUM> to <NUM> parts by weight, more preferably <NUM> to <NUM> parts by weight, per <NUM> parts by weight of the polyurethane. Suitable tackifiers are, for example, those based on natural resins, such as rosins, for example. Tackifiers based on natural resins include the natural resins themselves and also their derivatives formed, for example, by disproportionation or isomerization, polymerization, dimerization or hydrogenation. They may be present in their salt form (with, for example, monovalent or polyvalent counterions (cations)), or, preferably, in their esterified form. Alcohols used for the esterification may be monohydric or polyhydric. Examples are methanol, ethanediol, diethylene glycol, triethylene glycol, <NUM> ,<NUM>,<NUM>-propanetriol, and pentaerythritol. Also finding use as tackifiers, furthermore, are phenolic resins, hydrocarbon resins, e.g., coumarone-indene resins, polyterpene resins, terpene oligomers, hydrocarbon resins based on unsaturated CH compounds, such as butadiene, pentene, methylbutene, isoprene, piperylene, divinylmethane, pentadiene, cyclopentene, cyclopentadiene, cyclohexadiene, styrene, alpha-methylstyrene, vinyltoluene. Also being used increasingly as tackifiers are polyacrylates which have a low molar weight. These polyacrylates preferably have a weight-average molecular weight (Mw) of below <NUM><NUM>. The polyacrylates are composed preferably to an extent of at least <NUM>%, more particularly at least <NUM>%, by weight of C1-C8 alkyl (meth)acrylates. Preferred tackifiers are natural or chemically modified rosins. Rosins are composed predominantly of abietic acid or derivatives thereof.

For improved surface wetting, the hotmelt may in particular comprise wetting assistants, examples being fatty alcohol ethoxylates, alkylphenol ethoxylates, sulfosuccinic esters, nonyl- phenol ethoxylates, polyoxyethylenes/-propylenes or sodium dodecyl-sulfonates. The amount is generally <NUM> to <NUM> parts by weight, more particularly <NUM> to <NUM> parts by weight, per <NUM> parts by weight of polymer (solid).

Suitable stabilizers are e.g. selected from the group encompassing wetting agents, cellulose, polyvinyl alcohol, polyvinylpyrrolidone, and mixtures thereof.

Another aspect of the present invention is directed to a method for preparing the UV-moisture dual cure polyurethane reactive hotmelt of the present invention, which comprises mixing the the polyurethane of the present invention with at least one photoinitiator.

The above mentioned at least one additive can also be added before, during or after the addition of the photoinitiator.

The resulted hotmelt is kept free from light and water.

A further aspect of the present invention is directed to a method for adhesively bonding substrates, wherein.

and the applied hotmelt is cured by UV light and moisture before or after the two substrates are contacted with one another. The substrates may be selected, for example, from polymer films, paper, metal foils, wood veneer, fiber nonwovens made of natural synthetic fibers, shaped solid articles, examples being shaped parts made of metal, painted metal, wood, woodbase materials, fiber materials or plastic. Particularly preferred first substrates are polymer films. Polymer films are, more particularly, flexible sheetlike plastics in a thickness of <NUM> millimeter to <NUM> millimeters, which can be rolled up. Polymeric films of this kind are produced typically by coating, casting, calendering or extrusion and are typically available commercially in rolls or are produced on site. They may be of single-layer or multilayer construction. The plastic of the polymer films is preferably a thermoplastic, e.g., polyesters, such as polyethylene terephthalate (PET), thermoplastic polyolefins (TPO) such as polyethylene, polypropylene, polyvinyl chloride, especially plasticized PVC, polyacetates, ethylene/vinylacetate copolymers (EVA), ASA (acrylonitrile/styrene/acrylate), PU (polyurethane), PA (polyamide), poly(meth)acrylates, polycarbonates, or their plastics alloys, including, in particular foamed PVC films and foamed thermoplastic polyolefin films (TPO). Particularly preferred are PVC and thermoplastic polyolefins (TPO). The shaped parts may also be moldings composed of synthetic or natural fibers or chips bound together by a binder to form a molding; also suitable in particular are moldings made of plastic, e.g., ABS. The moldings may have any desired shape.

The substrates or moldings can be coated with the hotmelt by customary application techniques, as for example by spraying, spreading, knife coating, die application, roll application or casting application methods.

The amount of hotmelt applied is preferably <NUM> to <NUM>/m<NUM>, more preferably <NUM> to <NUM>/m<NUM>, very preferably <NUM> to <NUM>/m<NUM>.

A further aspect of the present invention is directed to a method for manufacturing a three-dimensional object by using the UV-moisture dual cure polyurethane reactive hotmelt of the present invention.

According to a preferred embodiment, the method for manufacturing a three-dimensional object comprises a step of forming a layer of UV-moisture dual cure polyurethane reactive hotmelt of the present invention and irradiating the layer with the UV light to set the layer, repeating the step until the three-dimensional object is formed.

According to one preferred embodiment, the method is an additive manufacturing method.

A further aspect of the present invention is directed to a three-dimensional object obtainable by the method of the present invention.

The UV-moisture dual cure polyurethane reactive hotmelt of the present invention has following advantages: low viscosity for fast and easy application; short setting time, and good green strength; and the cured product, especially the three-dimensional object produced from the hotmelt by the additive manufacturing method has high toughness (high impact strength).

<NUM> crystalline Polyester polyol, <NUM> non-crystalline Polyester polyol, and <NUM> crystalline Polyether polyol were added into a <NUM> reactor. Then, the reactor was sealed. The polyols were heated to <NUM> to melt all the polyols.

The polyols were dried under dynamic vacuum under mechanically stirring until there were no visible bubbles.

<NUM> diisocyanate with carbon-carbon double bonds on the side chain and <NUM> <NUM>,<NUM>'-MDI were added into the reactor under mechanically stirring.

The reactants were heated to <NUM> and the temperature was maintained for <NUM> hours under mechanically stirring, to produce the polyurethane.

<NUM> photoinitiator was added to the polyurethane and the mixture was stirred for another <NUM> hour to ensure uniform distribution of the photoinitiator in the polyurethane. Finally, the UV-moisture dual cure PU reactive hotmelt (RHM) was obtained.

The UV-moisture dual cure PU RHM was packed into aluminium bags and sealed under vacuum. The aluminium bags were stored in dark.

The green strength, setting time and open time of the UV-moisture dual cure PU RHM were tested according to the above mentioned methods, the testing results and the NCO content are shown in Table <NUM>. The setting time and open time of the UV-moisture dual cure PU RHM without applying UV irradiation were <NUM> and <NUM> respectively. The viscosity of the UV-moisture dual cure PU RHM was tested according to the above mentioned methods and the results were shown in table <NUM>. The impact strength is shown in table <NUM>.

<NUM> crystalline Polyester polyol and <NUM> non-crystalline Polyester polyol were added into a <NUM> reactor. Then, the reactor was sealed. The polyols were heated to <NUM> to melt all the polyols.

<NUM> diisocyanate with carbon-carbon double bonds on the side chain was added into the reactor under mechanically stirring.

<NUM> photoinitiator was added to the polyurethane and the mixture was stirred for another <NUM> hour to ensure uniform distribution of the photoinitiator in the polyurethane. Finally, the UV-moisture dual cure PU RHM was obtained.

The green strength, setting time and open time of the UV-moisture dual cure PU RHM were tested according to the above mentioned methods and the testing results and NCO content are shown in Table <NUM>. Both the setting time and open time of the UV-moisture dual cure PU RHM without applying UV irradiation were <NUM>. The viscosity of the UV-moisture dual cure PU RHM was tested according to the above mentioned methods and the results are shown in table <NUM>.

<NUM> crystalline Polyester polyol were added into a <NUM> reactor. Then, the reactor was sealed. The polyol was heated to <NUM> to melt all the polyols.

The polyol was dried under dynamic vacuum under mechanically stirring until there were no visible bubbles.

The NCO content of the UV-moisture dual cure PU RHM was <NUM> wt%. The setting time and open time of the UV-moisture dual cure PU RHM were tested according to the above mentioned methods. When the UV irradiating time was <NUM> (UV irradiation dose <NUM> mJ/cm<NUM>), the setting time was <NUM> and the open time was <NUM>. When the UV irradiating time was reduced to <NUM> (UV irradiation dose <NUM> mJ/cm<NUM>), the setting time and open time mantianed unchanged. The viscosity of the UV-moisture dual cure PU reactive hotmelt was tested according to the above mentioned methods and the result is shown in table <NUM>.

<NUM> crystalline Polyester polyol and <NUM> crystalline Polyether polyol were added into a <NUM> reactor. Then, the reactor was sealed. The polyols were heated to <NUM> to melt all the polyols.

The NCO content of the UV-moisture dual cure PU RHM was <NUM> wt%. The setting time and open time of the UV-moisture dual cure PU RHM were tested according to the above mentioned methods. When the UV irradiating time was <NUM> (UV irradiation dose <NUM> mJ/cm<NUM>), the setting time was <NUM> and the open time was <NUM>. The viscosity of the UV-moisture dual cure PU reactive hotmelt was tested according to the above mentioned methods and the result is shown in table <NUM>.

<NUM> crystalline Polyester polyol, <NUM> non-crystalline Polyester polyol, and <NUM> crystalline Polyether polyol were added into a <NUM> reactor; Then, the reactor was sealed; polyols were heated to <NUM> to melt all the polyols.

The polyols were dried under dynamic vacuum udder mechanically stirring until there were no bubbles visible.

<NUM> <NUM>,<NUM>'- MDI was added to the reactor under mechanically stirring.

The reactants were heated to <NUM> and the temperature was maintained for <NUM> hours under mechanically stirring, to produce the standard polyurethane, i.e. the standard PU RHM.

The standard PU RHM was packed into aluminium bags and sealed under vacuum. The aluminium bags were stored in dark.

The green strength, setting time and open time of the standard PU RHM were tested according to the above mentioned methods and the testing results and NCO content are shown in Table <NUM>. The viscosity of the standard PU RHM was tested according to the above mentioned method and the results were shown in table <NUM>. The impact strength is shown in table <NUM>.

The production of prepolymer: <NUM> HDI trimer (Basonat HI) was reacted with <NUM> Hydroxyethyl methacrylate at <NUM> for <NUM>, the resulted prepolymer has an NCO content of <NUM>%.

<NUM> crystalline Polyester polyol, <NUM> non-crystalline Polyester polyol, and <NUM> crystalline Polyether polyol were added into a <NUM> reactor. Then, the reactor was sealed; the polyols were heated to <NUM> to melt all the polyols.

The polyols were dried under dynamic vacuum under mechanically stirring until there were no bubbles visible.

<NUM> prepolymer prepared above and <NUM> <NUM>,<NUM>'- MDI were added to the reactor under mechanically stirring. The reactants were heated to <NUM> and the temperature was maintained for <NUM> hours under mechanically stirring, to produce the polyurethane.

<NUM> photo initiator was added to the polyurethane and the mixture was stirred for another <NUM> hour to ensure uniform distribution of the photoinitiator in the polyurethane. Finally, the UV-moisture dual cure PU RHM was obtained.

The green strength, setting time and open time of the UV-moisture dual cure PU RHM were tested according to the above mentioned methods and the testing results and NCO content are shown in Table <NUM>. The setting time and open time of the UV-moisture dual cure PU RHM without applying UV irradiation were <NUM> and <NUM> respectively. The viscosity of the UV-moisture dual cure PU RHM was tested according to the above mentioned method and the results were shown in table <NUM>. The impact strength is shown in table <NUM>.

The viscosities of the UV-moisture dual cure PU RHM from example <NUM> is similar with that of the standard PU RHM from comparative example <NUM>; however, the viscosity of the UV-moisture dual cure PU RHM from comparative example <NUM> is much higher than those of standard PU RHM and the UV-moisture dual cure PU RHMs from examples <NUM> to <NUM>. The high viscosity is disadvantageous to the application of the hotmelt.

The setting time of the UV-moisture dual cure PU RHM from example <NUM> without UV irradiation is <NUM>, however it can be set within <NUM> upon applying <NUM>-UV irradiation, this property is advantageous to hotmelt. In examples <NUM> and <NUM>, even the UV irradiating times were further reduced, the setting time, open time or green strength mantianed unchanged comparing with a <NUM> UV irradiation time, which means the UV-moisture dual cure PU RHM from examples <NUM> and <NUM> have higher reactivity.

The UV-moisture dual cure PU RHM from example <NUM> can remain tacky for up to <NUM> (open time).

The dual cure PU RHMs from examples <NUM> and <NUM> have excellent green strength, especially the Dual cure PU RHM from example <NUM>.

Claim 1:
An UV-moisture dual cure polyurethane reactive hotmelt comprising (i) at least one polyurethane which has an isocyanate group and has C-C double bonds on the side chain and (ii) at least one photoinitiator, wherein the isocyanate in the isocyanate component for synthesizing the polyurethane is diisocyanate and the isocyanate component comprises at least one diisocyanate having C-C double bonds on the side chain.