flexible polyurethane foams have generally an open cell structure exhibiting high air - permeability ( air - flow ) and reversible deformability , as described by gunter oertel ( polyurethane handbook , pp . 161 - 233 ) and keiji iwata ( poriuretan jushi handobukk ( polyurethane resin handbook ), pp . 150 - 221 ). the physical properties of a flexible polyurethane foam depend on the chemical structure of the starting polyol and isocyanate , amount of the blowing agent , the chemical factors such as the isocyanate index , the intended cell structure , etc . generally , as shown in the above cited polyurethane handbook , pp . 184 - 191 and pp . 212 - 218 , and poriuretan jushi handobukk , pp . 160 - 166 and pp . 186 - 191 , the flexible polyurethane foam has a density ranging from 10 to 100 kg / m 3 ( jis k 6401 ), a compression strength ( idl 25 %) ranging from 2 to 80 kgf ( 20 to 800n ) ( jis k 6401 ), and an elongation ranging from 80 to 500 % ( jis k 6301 ), but are not limited thereto . the flexible polyurethane foam of the present invention includes semi - rigid polyurethane foam in view of the starting materials and foam properties . semi - rigid polyurethane foams , as shown in the above cited polyurethane handbook , pp . 223 - 233 , and poriuretan jushi handobukk , pp . 211 - 221 , have an open cell structure similar to flexible polyurethane foams exhibiting high air - permeability and reversible deformability although the foam density and compression strength are higher than those of the flexible polyurethane foam . the starting polyol and isocyanate are similar to the flexible polyurethane foam . therefore , the semi - rigid polyurethane foams are generally included in flexible polyurethane foams . the semi - rigid polyurethane foam has generally a density ranging from 40 to 800 kg / m 3 , 25 %- compression strength ranging from 0 . 1 to 2 kgf / cm 2 ( 9 . 8 to 200 kpa ), and an elongation ranging from 40 to 200 %. the properties , however , are not limited thereto . the rigid polyurethane foam of the present invention has a highly crosslinked closed cell structure and is not capable of being reversible deformation , and has properties quite different from the properties of flexible foams , and semi - rigid foams , as shown in the above cited polyurethane handbook , pp . 234 - 313 , and poriuretan jushi handobukk , pp . 224 - 283 . the rigid foam has generally a density ranging from 20 to 100 kg / m 3 , and a compression strength ranging from 0 . 5 to 10 kgf / cm 2 ( 50 to 1000 kpa ), but the properties are not limited thereto . the amine catalyst of the present invention is a compound represented by general formula ( 1 ) above , wherein the group a may be linear or branched . the long - chain aliphatic monoamine having the group a of 11 to 14 carbons is exemplified by dimethyldodecylamine , dimethyltetradecylamine , etc . the monoamines of 10 carbons or lower emit amine odor and are highly volatile . therefore , working environment cannot readily be improved with such lower monoamine , or emission of the lower amine cannot be prevented , and the curing rate is low and productivity of the urethane foam is low with the lower amine . on the other hand , the monoamine of 15 carbons or higher exhibits remarkably lower catalytic activity and lower curing properties , and needs to be used in a larger amount , which is disadvantageous in cost and productivity of polyurethane foams . the long - chain aliphatic diamine having the group a of 10 to 15 carbons is exemplified by tetramethyl - decane - diamine , tetramethyl - undecane - diamine , tetramethyl - dodecane - diamine , tetramethyl - tetradecane - diamine , etc . the diamines of 9 carbons or lower emit amine odor and exhibit high volatility . therefore , working environment cannot readily be improved with such lower diamine , or emission of the lower amine cannot be prevented , although such a diamine is effective to improve the curing rate of the foam . on the other hand , a diamine of 16 carbons or higher exhibits remarkably lower catalytic activity and a lower curing rate , and needs to be used in a larger amount , which is disadvantageous in production of polyurethane . the amine catalyst of the present invention may be produced by any known conventional method , and the production process thereof is not specially limited . for example , it can be produced readily by reduction methylation of a starting monoamine or diamine . the amine catalyst represented by general formula ( 1 ) is preferably used in combination with other gelling catalyst and / or a blowing catalyst in the present invention . the gelling catalyst means a tertiary amine catalyst which accelerates particularly the reaction of a polyisocyanate and a polyol , and are exemplified by triethylenediamine , 1 , 8 - diazabicyclo [ 5 . 4 . 0 ] undecene - 7 , and imidazoles such as 1 - methylimidazole , 1 , 2 - dimethylimidazole , and 1 - isobutyl - 2 - methylimidazole etc . the blowing catalyst means a tertiary amine catalyst which accelerates particularly the reaction of an isocyanate with water to evolve carbon dioxide effectively , and are exemplified by bis ( 2 - dimethylaminoethyl ) ether , n , n , n &# 39 ;, n &# 34 ;, n &# 34 ;- pentamethyldiethylenetriamine , n , n , n &# 39 ;, n &# 34 ;, n &# 39 ;&# 34 ;, n &# 39 ;&# 34 ;- hexamethyltriethylenetetramine , etc . the composition of the amine catalyst of the present invention ( represented by general formula ( 1 )) and the gelling catalyst contains preferably 20 to 95 % by weight of the amine catalyst of the present invention and 80 to 5 % by weight of the gelling catalyst based on the total amount of the catalyst . at the ratio of the gelling catalyst of not more than 80 % by weight , the curing rate , the flowability , and the moldability of the foam are improved , whereas at the ratio thereof of not less than 5 % by weight , the total amount of the catalyst can be reduced , which is advantageous in production cost . the composition of the amine catalyst of the present invention ( represented by general formula ( 1 )) and the blowing catalyst contains preferably 40 to 99 % by weight of the amine catalyst of the present invention and 60 to 1 % by weight of the blowing catalyst based on the total amount of the catalyst . at the ratio of the blowing catalyst of not more than 60 % by weight , the initial foaming rate is appropriate , the liquid flowability is maintained , and the curing rate , the moldability , and the surface adhesion properties of the rigid foams are improved , whereas at the ratio thereof of not less than 1 % by weight the foam - flowability is improved and the total amount of the catalyst is reduced , which is advantageous in production cost . when both of the gelling catalyst and the blowing catalyst are combined with the amine catalyst of the present invention ( represented by general formula ( 1 )), the catalyst mixture contains preferably 19 to 90 % by weight of the amine catalyst of the present invention , 80 to 5 % by weight of the gelling catalyst , and 60 to 1 % by weight of the blowing catalyst . the amine catalyst of the present invention may be combined with a cocatalyst including other tertiary amines , tertiary amine compounds having an active hydrogen reactive to the isocyanate , organometal compounds , and / or metal carboxylates for polyurethane production . the above mentioned other tertiary amines combined with the catalyst of the present invention include tertiary amines such as triethylamine , n , n - dimethylcyclohexylamine , n , n , n &# 39 ;, n &# 39 ;- tetramethylethylenediamine , n , n , n &# 39 ;, n &# 39 ;- tetramethylpropylenediamine , n , n , n &# 39 ;, n &# 34 ;, n &# 34 ;- pentamethyl -( 3 - aminopropyl ) ethylenediamine , n , n , n &# 39 ;, n &# 34 ;, n &# 34 ;- pentamethyldipropylenetriamine , n , n , n &# 39 ;, n &# 39 ;- tetramethylguanidine , 1 , 3 , 5 - tris ( n , n - dimethylaminopropyl ) hexahydro - s - triazine , n , n , n &# 39 ;, n &# 39 ;- tetramethylhexamethylenediamine , n - methyl - n &# 39 ;-( 2 - dimethylaminoethyl ) piperazine , n , n &# 39 ;- dimethylpiperazine , n - methylpiperazine , n - methylmorpholine , and n - ethylmorpholine etc . the above mentioned tertiary amine compounds having an active hydrogen include alkanolamines such as n , n - dimethylaminoethanol , n , n - dimethylaminoisopropanol , n , n - dimethylaminoethoxyethanol , n , n , n &# 39 ; trimethylaminoethylethanolamine , n , n , n &# 39 ;- trimethyl - n &# 39 ;- hydroxyethyl - bisaminoethyl ether , n , n - bis ( 3 - dimethylaminopropyl )- n - isopropanolamine , n -( 3 - dimethylaminopropyl )- n , n - diisopropanolamine , n -( 2 - hydroxyethyl )- n &# 39 ;- methylpiperazine , and n , n - dimethylaminohexanol ; and amine compounds having both a primary amino group and a secondary amino group such as dimethylaminopropylamine , and bis ( dimethylaminopropyl ) amine . such an amine compound having active hydrogen reacts with the isocyanate to be incorporated into the foam , thereby reducing volatilization of amine . the amine catalyst of the present invention may be combined with an organometal compound and / or a metal carboxylate as a cocatalyst . the organometal compound includes stannous diacetate , stannous dioctoate , stannous dioleate , stannous dilaurate , dibutyltin oxide , dibutyltin diacetate , dibutyltin dilaurate , dibutyltin dichloride , dioctyltin dilaurate , lead octanoate , lead naphthenate , nickel naphthenate , and cobalt naphthenate . of these organometal compounds , organotin compounds are preferred , stannous dioctate and dibutyltin dilaurate being more preferred . the metal caoboxylate includes alkali metal salts or alkaline earth metal salts of carboxylic acids . the carboxylic acid includes aliphatic mono - and di - carboxylic acids such as acetic acid , propionic acid , 2 - ethylhexanoic acid , and adipic acid ; aromatic mono - and di - carboxylic acids such as benzoic acid , and phthalic acid , but are not limited thereto . the salt - forming alkali metal includes lithium , sodium , and potassium ; and the salt - forming alkaline earth metal includes calcium , and magnesium , but the metal is not limited thereto . the usual amount of the catalyst of the present invention in polyurethane production is generally in the range of from 0 . 01 to 10 parts by weight based on 100 parts by weight of the polyol , but is not limited thereto . the amount of the aforementioned other amine catalyst , the organometal compound , and the metal carboxylate to be used in combination with the amine catalyst of the present invention is generally in the range of from 0 . 01 to 5 parts by weight , but is not limited thereto . further , an organic carboxylic acid salt of the amine compound of the present invention , and an organic carboxylic acid salt of the aforementioned tertiary amine may be used suitably as the catalyst and the cocatalyst provided that the function as the catalyst of the present invention is not impaired . the amine catalyst of the present invention may be used singly or in combination with other amine catalyst as described above . in mixing of the catalyst components , a solvent such as dipropylene glycol , ethylene glycol , 1 , 4 - butanediol and water may be used , if necessary . the solvent is used in an amount preferably of not more than 70 % by weight of the entire catalyst components , but the amount is not limited thereto . the catalyst thus prepared may be added to the polyol . otherwise , respective amine catalyst component may be separately added to the polyol . the method of the catalyst addition is not specially limited . the polyol which is useful in the polyurethane production with the amine catalyst of the present invention includes generally known polyesterpolyols , polyetherpolyols , polymerpolyols , and mixtures thereof . the known polyesterpolyols are derived from a dibasic acid and a polyhydric alcohol . the known polyetherpolyols are derived by addition reaction of ethylene oxide , propylene oxide or the like to a polyhydric alcohol such as glycol , glycerin , pentaerythritol , trimethylolpropane , sorbitol , and sucrose ; an aliphatic amine such as ammonia , ethylenediamine , and ethanolamines ; or aromatic amines such as toluenediamine , and diphenylmethane - 4 , 4 &# 39 ;- diamine , or a mixture thereof . the known polymer polyols are derived by reaction of the polyetherpolyol with an ethylenic unsaturated monomer such as butadiene , acrylonitrile , and styrene in the presence of a radical polymerization initiator . in the production of a flexible polyurethane foam , the polyol is preferably a polyetherpolyol and / or a polymer - polyol . the polyol has an average functionality ranging preferably from 2 to 5 , and an average hydroxyl number ranging preferably from 20 to 100 mgkoh / g , more preferably from 20 to 80 mgkoh / g , and contains oxyethylene groups at a content preferably not more than 90 %. incidentally , the flexible polyurethane herein includes semi - rigid polyurethane foams since the starting polyol is the same . in the production of a rigid polyurethane foam , the polyol has an average functionality ranging usually from 4 to 8 , and an average hydroxyl number ranging preferably from 200 to 800 mgkoh / g , more preferably from 300 to 700 mgkoh / g . the polyisocyanate useful in the polyurethane foam production with the catalyst of the present invention may be any known polyisocyanate , including aromatic polyisocyanates such as toluene diisocyanate ( tdi ), 4 , 4 &# 39 ;-, or 4 , 2 &# 39 ;- diphenylmethane diisocyanate ( mdi ), naphthylene diisocyanate , and xylylene diisocyanate ; alicyclic polyisocyanates such as isophorone diisocyanate ; aliphatic polyisocyanates such as hexamethylene diisocyanate ; free isocyanate - containing prepolymer derived by reaction of a polyol with the above polyisocyanate ; modified polyisocyanate such as carbodimide - modified polyisocyanates ; and mixtures thereof . of these , preferred are tdi and derivatives thereof , and mdi and derivatives thereof , and mixtures thereof . tdi and derivatives include mixtures of 2 , 4 - tdi and 2 , 6 - tdi , and tdi - terminated isocyanate prepolymer derivatives . mdi and derivatives thereof includes mixtures of mdi and its polymer , polyphenylmethylene isocyanate ( so - called polymeric - mdi ), and / or isocyanate - terminated diphenylmethane diisocyanate derivatives . in the production of polyurethane foam , by use of the catalyst of the present invention foam , any physical or chemical blowing agent excluding chlorofluorocarbons ( cfcs ) is useful . in the production of rigid polyurethane foam , water is indispensable as a blowing agent . the known physical blowing agents include hydrocarbons such as pentane , and cyclopentane ; hydrochlorofluorocarbons such as hcfc - 22 , and 141b ; hydrofluorocarbons such as hfc - 134a , 245 and 356 ; air , nitrogen , and carbon dioxide , and their mixtures . the known chemical blowing agents include water , organic acids , inorganic acids like boric acid , alkali carbonates , cyclic carbonates , dialkyl carbonates , etc . which evolve gas by reaction with polyurethane resin components or by decomposition on heating , etc . in the production of flexible polyurethane foams , water is preferred as a blowing agent . the amount of water is preferably in the range of from 2 to 10 parts by weight , more preferably from 2 to 7 parts by weight based on 100 parts by weight of the polyol . in the production of rigid polyurethane foams , the blowing agent includes water , and mixtures of water with a hydrocarbon , a hydrochlorofluorocarbon , or a hydrofluorocarbon . the amount of water is preferably in the range of from 2 to 15 parts by weight , more preferably from 2 to 10 parts by weight based on 100 parts of the polyol . with excessive amount of water , the curing rate becomes lower , the blowing process range becomes narrower , the foam density becomes lower , or the moldability becomes worse . the amount of the hydrocarbon , the hydrochlorofluorocarbon , or the hydrofluorocarbon to be combined with the water is suitably selected depending on the desired density of the foam , and is preferably not more than 40 parts by weight , more preferably not more than 30 parts by weight based on 100 parts by weight of the polyol , but is not limited thereto . the foam stabilizer employed in the present invention may be any known one , and is exemplified by nonionic surfactants such as organosiloxanepolyoxyalkylene copolymers , and silicone - grease copolymers , and mixtures thereof . the amount thereof to be used is usually in the range of from 0 . 1 to 10 parts by weight based on 100 parts by weight of the polyol . a crosslinking agent or a chain extender may be added , if necessary , in the present invention . the crosslinking agent or the chain extender includes low - molecular polyhydric alcohols such as ethylene glycol , diethylene glycol , 1 , 4 - butanediol , and glycerin ; low - molecular amine polyol such as diethanolamine , and triethanolamine ; polyamines such as ethylene diamine , xylylenediamine , and methylene - bis ( o - chloroaniline ); and the like . further , a coloring agent , a flame retardant , an antioxidant , or other known additives may be added to the polyurethane foam of the present invention in conventional amounts . the amine catalyst for polyurethane production of the present invention , which has a higher molecular weight and a lower vapor pressure than conventional amine catalysts , emits extremely less odor , thereby improving working environment for polyurethane production significantly , and giving no residual odor and reducing the volatile matter in the produced polyurethane foam . furthermore , in the formulation with less amount of cfc and larger amount of water , the amine catalyst of the present invention raises curing rate of the foam and improves the moldability , thereby improving remarkably the productivity and yield of the foam . the present invention is described below in more detail by reference to examples and comparative examples without limiting the invention in any way . polyurethane foams were prepared with the starting materials and the foaming conditions shown below . the resulting foams were tested for physical properties . the flexible polyurethane foams were tested for moldability and curing rate in the manner as shown later . the results are shown in tables 1 to 4 . ______________________________________polyol a . sup . 1 ) 60 . 0 ( parts by weight ) polyol b . sup . 2 ) 40 . 0water 2 . 7foam stabilizer . sup . 3 ) 2 . 0amine catalyst . sup . 4 ) changedisocyanate . sup . 5 ) index = 105______________________________________ 1 ) polyetherpolyol ( fa - 703 , produced by sanyo chemical industries , ltd ., oh number = 34 mgkoh / g ) 2 ) polymer polyol ( fa - 728r , produced by sanyo chemical industries , ltd ., oh number = 28 mg / koh / g ) teda - l33 : 33 . 3 % triethylenediamine solution in dipropylene glycol ( produced by tosoh corporation ) toyocat - et : 70 % bis ( 2 - dimethylaminoethyl ) ether solution in dipropylene glycol ( produced by tosoh corporation ) 5 ) tdi / crude mdi = 80 / 20 ( tdi : 2 , 4 - tdi / 2 , 6 - tdi = 80 / 20 , produced by nippon polyurethane industry co ., ltd ), ( crude mdi : mr - 200 produced by nippon polyurethane industry co ., ltd .) the starting material mixture for polyurethane was poured into 2 - liter polyethylene cup and allowed to blow at room temperature ( 20 ° to 25 ° c .). the reactivity , foam density , etc . were measured with the resulting polyurethane . density ( kg / m 3 ) of a test specimen of 6 × 6 × 8 cm cut out from the center portion of the foam the starting material mixture of polyurethane foam was poured into an aluminum mold ( internal dimension : 50 × 30 × 10 cm ) having a portion for a thin part ( 10 × 30 × 0 . 5 cm ) adjusted to 50 ° c ., and allowed to foam therein . after 5 . 5 minutes , the upper lid of the mold was taken out , and the thin part of the foam was compressed with a marker ( 20 mm in diameter , about 2 . 5 kg in weight ) repeatedly for 5 seconds at intervals of 10 seconds on the different position of the foam . the time elapsed from the starting time of mixing before no mark of compression come to be observed was defined as the curing rate ( minutes ). the above foam having blown in the mold was evaluated for void formation , skin roughness , skin exfoliation on three grades : the starting material mixture of polyurethane foam was poured into an aluminum mold ( internal dimension : 30 × 30 × 10 cm ) kept at 50 ° c ., and was allowed to foam therein . 7 minutes later , the resulting foam was taken out from the mold , and was immediately subjected to crushing treatment . the foam was aged at room temperature for 24 hours . after the aging , four test pieces ( 70 × 70 × 60 mm ) were cut out from the core portion of the foam . the dimension of the test pieces were measured precisely . the test pieces were compressed to the size of 50 %, and were aged in an oven at a temperature of 70 ° c . and humidity of 95 % for 22 hours . then the test pieces were left standing at room temperature for 30 minutes . the dimensions of the test pieces were measured , and the compression set was calculated by the equation below : 5 . 0 parts by weight of the catalyst was mixed with 100 parts by weight of a polyol ( fa703 ). the mixture was smelled by 10 persons , and the degree of the odor was evaluated based on the standard below . in the case of combined catalysts , 5 . 0 parts by weight of the combined catalyst was mixed with 100 parts by weight of the polyol . medium : 4 or more out of 10 persons perceive weak odor faint : 3 or less out of 10 persons perceive faint odor tables 1 to 4 clearly show that use of the specified long chain aliphatic monoamine or diamine as the amine catalyst has a reduced odor of the catalyst , and enables flexible polyurethane foam production with excellent moldability at high curing rate . combination of this catalyst with a gelling catalyst or a blowing catalyst enables reduction of the total amount of the required catalysts without impairing the catalytic activity , and is effective in improving wet heat compression set in comparison with single use of the catalyst of the present invention . on the other hand , in comparative examples 1 , and 4 to 6 , conventional amine catalysts , and low molecular amine catalysts such as nem , tea , and dmea emit strong odor , not giving high curing rate , and not giving sufficient moldability , thereby involving disadvantages in working environment and foam productivity . in comparative examples 2 , 3 , 7 , and 8 , the amine catalysts having a skeleton analogous to that of the amine of the present invention were not effective in improvement of catalyst odor , curing rate , moldability , and wet - heat compression set without achieving the intention . polyurethane foams were prepared with the formulations below and under the same foaming conditions as in examples 1 to 5 . the resulting rigid polyurethane foams were tested for properties . the flowability , the adhesion strength , and the dimensional stability were measured by the methods below . the results are shown in tables 5 to 8 . ______________________________________polyol c . sup . 6 ) 50 . 0 ( parts by weight ) polyol d . sup . 7 ) 50 . 0water 4 . 0hcfc - 141b 11 . 0foam stabilizer . sup . 8 ) 1 . 5amine catalyst . sup . 9 ) changedisocyanate . sup . 10 ) index = 110______________________________________ 6 ) polyetherpolyol ( nt - 400 , produced by mitsui toatsu chemicals , inc ., oh number = 390 mgkoh / g ) 7 ) polyetherpolyol ( su - 464 , produced by mitsui toatsu chemicals , inc ., oh number = 450 mg / koh / g ) the starting material mixture for the polyurethane was poured into 2 - liter polyethylene cup and allowed to blow at room temperature ( 20 ° to 25 ° c .). the reactivity , free blowing density , etc . were measured . tack - free time : time before dissipation of stickiness of the top surface ( seconds ) the hardness of the upper surface of freely blown foam was measured with a shore c hardness meter . the higher hardness means higher curability . a freely blown foam was prepared in an aluminum mold ( 50 × 4 . 5 × 50 cm ), and the density ( kg / m 3 ) was measured . the lower density means the higher flowability . a foam was prepared in an aluminum mold ( 25 × 8 × 25 cm ) kept at 30 ° c . and in which a galvanized sheet iron ( 50 × 50 mm ) was placed on its inside lateral face . ten minutes after the blowing , 90 ° peel strength ( kg / 25cm 2 ) was measured as the adhesion strength . a freely blown foam was prepared in an aluminum mold ( 25 × 8 × 25 cm ). the core portion was cut out in a size of 20 × 6 × 20 cm ) was subjected to aging at 20 ° c . for 70 days . the volume change (%) by the aging was measured . the odor was evaluated in the same manner as in examples 1 to 5 . tables 5 to 8 clearly show that the use of the specified long - chain aliphatic monoamine or diamine as the amine catalyst reduces the odor of the catalyst , and enables rigid polyurethane foam production with excellent foam properties at high curing rate . with a formulation in which a smaller amount of a hydrofluorocarbon was used in place of cfcs and an increased amount of water was used , a foam could be produced with high foam flowability , high adhesion strength , and high dimensional stability . further , combination of this catalyst with a gelling catalyst or a blowing catalyst enabled reduction of the total amount of the required catalysts without impairing the catalytic activity . the combination with a gelling catalyst enabled formation of a foam with high curing rate and a high dimensional stability , while the combination with a blowing catalyst enabled foam production with high flowability , low density , and high dimensional stability . on the other hand , in comparative examples 10 and 11 , a conventional gelling catalyst and / or blowing catalyst without the catalyst of the present invention , the foam flowability was poor and the properties of the foam were inferior . conventionally employed low molecular amines such as dmcha used for rigid foam production emited strong odor , giving low curing rate and low adhesion strength , involving disadvantages in working environment and foam productivity . mdcha , a high molecular amine catalyst , emitted less odor , but gave low curing rate and low adhesion strength disadvantageously . in comparative examples 12 , 13 , 16 , and 17 , the amine catalysts having a skeleton analogous to that of the amine of the present invention were not effective in improvement of catalyst odor , curing rate , and foam forming properties without achieving the intention . table 1______________________________________ example 1 2 3 4 5______________________________________catalyst ( parts by weight ) * teda - l33 -- 0 . 52 -- 0 . 32 0 . 32toyocat - et -- -- 0 . 30 0 . 08 0 . 08dmdoa 2 . 40 1 . 20 1 . 20 1 . 20 -- dmtda -- -- -- -- 1 . 35dmoa -- -- -- -- -- dmhda -- -- -- -- -- nem -- -- -- -- -- tea -- -- -- -- -- dmea -- -- -- -- -- reactivity ( seconds ) cream time 9 9 7 8 8gel time 82 80 80 79 80rise time 120 115 113 114 115foam propertiesfree density ( kg / m . sup . 3 ) 41 . 2 40 . 1 40 . 8 40 . 4 40 . 7mold density ( kg / m . sup . 3 ) 50 . 8 50 . 5 50 . 9 50 . 8 50 . 5moldability 1 1 2 1 1curing rate ( min ) 6 &# 39 ; 50 &# 34 ; 6 &# 39 ; 40 &# 34 ; 6 &# 39 ; 50 &# 34 ; 6 &# 39 ; 40 &# 34 ; 6 &# 39 ; 40 &# 34 ; wet - heat compression 18 . 5 16 . 5 17 . 2 16 . 5 17 . 0set (%) odor ** none fnt fnt fnt fnt______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint table 2______________________________________ comparative example 1 2 3 4 5 6______________________________________catalyst ( parts by weight ) * teda - l33 0 . 61 0 . 32 0 . 32 0 . 32 0 . 32 0 . 32toyocat - et 0 . 15 0 . 08 0 . 08 0 . 08 0 . 08 0 . 08dmdoa -- -- -- -- -- -- dmtda -- -- -- -- -- -- dmoa -- 0 . 80 -- -- -- -- dmhda -- -- 1 . 50 -- -- -- nem -- -- -- 3 . 30 -- -- tea -- -- -- -- 0 . 76 -- dmea -- -- -- -- -- 0 . 75reactivity ( seconds ) cream time 7 9 8 8 8 7gel time 80 81 79 79 80 79rise time 115 115 117 117 115 107foam propertiesfree density ( kg / m . sup . 3 ) 40 . 8 40 . 6 40 . 5 40 . 9 40 . 4 40 . 6mold density ( kg / m . sup . 3 ) 50 . 3 50 . 5 50 . 6 50 . 7 50 . 8 50 . 6moldability 3 1 2 3 1 4curing rate ( min ) 7 &# 39 ; 50 &# 34 ; 8 &# 39 ; 00 &# 34 ; 7 &# 39 ; 50 &# 34 ; 7 &# 39 ; 50 &# 34 ; 7 &# 39 ; 00 &# 34 ; 8 &# 39 ; 0wet - heat compression 18 . 0 19 . 0 19 . 5 20 . 5 18 . 0 22 . 0set (%) odor ** med strg fnt strg strg strg______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint table 3______________________________________ example 6 7 8 9 10______________________________________catalyst ( parts by weight ) * teda - l33 -- -- 0 . 32 0 . 32 0 . 32toyocat - et -- -- 0 . 08 0 . 08 0 . 08tmdda 0 . 98 -- 0 . 47 -- -- tmunda -- 1 . 05 -- 0 . 52 -- tmdoda -- -- -- -- 0 . 57tmhmda -- -- -- -- -- tmhdda -- -- -- -- -- nem -- -- -- -- -- dmea -- -- -- -- -- reactivity ( seconds ) cream time 9 9 9 8 8gel time 80 81 79 80 80rise time 111 113 110 112 115foam propertiesfree density ( kg / m . sup . 3 ) 40 . 4 40 . 5 40 . 0 40 . 5 40 . 9mold density ( kg / m . sup . 3 ) 50 . 1 50 . 6 50 . 5 50 . 6 50 . 8moldability 1 1 1 1 1curing rate ( min ) 6 &# 39 ; 30 &# 34 ; 6 &# 39 ; 20 &# 34 ; 6 &# 39 ; 30 &# 34 ; 6 &# 39 ; 30 &# 34 ; 6 &# 39 ; 50 &# 34 ; wet - heat compression 16 . 5 17 . 0 16 . 5 16 . 8 16 . 5set (%) odor ** none none fnt fnt fnt______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint table 4______________________________________ comparative example 1 7 8 4 6______________________________________catalyst ( parts by weight ) * teda - l33 0 . 61 0 . 32 0 . 32 0 . 32 0 . 32toyocat - et 0 . 15 0 . 08 0 . 08 0 . 08 0 . 08tmdda -- -- -- -- -- tmunda -- -- -- -- -- tmdoda -- -- -- -- -- tmhmda -- 0 . 35 -- -- -- tmhdda -- -- 0 . 75 -- -- nem -- -- -- 3 . 30 -- dmea -- -- -- -- 0 . 75reactivity ( seconds ) cream time 7 8 8 8 7gel time 80 79 80 79 79rise time 115 112 115 117 107foam propertiesfree density ( kg / m . sup . 3 ) 40 . 8 40 . 6 40 . 5 40 . 9 40 . 6mold density ( kg / m . sup . 3 ) 50 . 3 50 . 6 50 . 5 50 . 7 50 . 6moldability 3 1 3 3 4curing rate ( min ) 7 &# 39 ; 50 &# 34 ; 6 &# 39 ; 30 &# 34 ; 7 &# 39 ; 50 &# 34 ; 7 &# 39 ; 50 &# 34 ; 8 &# 39 ; 0wet heat compression 18 . 0 18 . 0 18 . 5 20 . 5 22 . 0set (%) odor ** med strg fnt strg strg______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint table 5______________________________________ comparative example example 11 12 13 14 15 9______________________________________catalyst ( parts byweight ) * teda - l33 -- 1 . 40 -- 0 . 71 0 . 71 2 . 80toyocat - -- -- 0 . 55 0 . 30 0 . 30 -- dtdmdoa 4 . 60 2 . 30 2 . 30 2 . 30 -- -- dmtda -- -- -- -- 2 . 55 -- dmoa -- -- -- -- -- -- dmhda -- -- -- -- -- -- dmcha -- -- -- -- -- -- mdcha -- -- -- -- -- -- reactivity ( seconds ) cream time 14 14 10 12 13 14gel time 50 50 50 50 50 50tack free time 64 63 62 64 63 63rise time 77 73 78 76 78 73foampropertiesfree density 26 . 5 26 . 7 26 . 3 26 . 4 26 . 5 27 . 9 ( kg / m . sup . 3 ) mold density ( kg / m . sup . 3 ) overall 29 . 5 29 . 7 28 . 0 28 . 7 28 . 8 31 . 8core 27 . 7 28 . 0 26 . 5 27 . 1 27 . 2 30 . 7curing rate 65 70 65 67 66 70 ( shore c ) adhesion 11 . 0 9 . 5 9 . 0 9 . 5 9 . 5 3 . 9strength ( kg / 25 cm . sup . 2 ) dimension 23 . 0 20 . 2 10 . 0 12 . 0 13 . 0 23 . 0stability (%) odor ** none fnt fnt fnt fnt med______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint table 6______________________________________ comparative example 10 11 12 13 14 15______________________________________catalyst ( parts by weight ) * teda - l33 -- 0 . 95 0 . 40 0 . 40 -- -- toyocat - dt 1 . 10 0 . 55 0 . 30 0 . 30 -- -- dmdoa -- -- -- -- -- -- dmtda -- -- -- -- -- -- dmoa -- -- 2 . 00 -- -- -- dmhda -- -- -- 3 . 00 -- -- dmcha -- -- -- -- 2 . 40 -- mdcha -- -- -- -- -- 11 . 0reactivity ( seconds ) cream time 7 10 11 11 13 12gel time 50 50 50 50 50 50tack free time 61 63 65 65 73 75rise time 80 74 79 77 78 85foam propertiesfree density ( kg / m . sup . 3 ) 26 . 3 26 . 8 26 . 7 26 . 4 26 . 6 27 . 0mold density ( kg / m . sup . 3 ) overall 30 . 0 29 . 7 29 . 7 30 . 2 29 . 2 30 . 3core 28 . 7 28 . 0 27 . 7 28 . 8 27 . 6 28 . 4curing rate ( shore c ) 50 58 58 55 60 20adhesion strength 1 . 4 3 . 2 6 . 0 6 . 0 3 . 3 1 . 2 ( kg / 25 cm . sup . 2 ) dimension stability (%) 9 . 4 20 . 0 30 . 0 27 . 5 24 . 1 7 . 3odor ** med med strg fnt strg fnt______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint table 7______________________________________ comparative example example 16 17 18 19 20 9______________________________________catalystparts byweight ) * teda - l33 -- 1 . 40 -- 0 . 71 0 . 71 2 . 80toyocat - -- -- 0 . 55 0 . 30 0 . 30 -- dttmdda 2 . 40 1 . 20 1 . 20 1 . 20 -- -- tmdoda -- -- -- -- 1 . 35 -- tmhmda -- -- -- -- -- -- tmhdda -- -- -- -- -- -- dmcha -- -- -- -- -- -- mdcha -- -- -- -- -- -- reactivity ( seconds ) cream time 14 14 10 12 12 14gel time 50 51 49 51 50 50tack free time 64 64 63 63 64 63rise time 75 73 75 76 75 73foampropertiesfree density 26 . 3 26 . 5 26 . 4 26 . 4 26 . 4 27 . 9 ( kg / m . sup . 3 ) mold density ( kg / m . sup . 3 ) overall 29 . 5 29 . 7 28 . 0 28 . 7 28 . 8 31 . 8core 27 . 7 28 . 0 26 . 5 27 . 1 27 . 2 30 . 7curing rate 64 69 66 68 67 70 ( shore c ) adhesion 10 . 5 10 . 0 9 . 0 9 . 5 9 . 5 3 . 9strength ( kg / 25 cm . sup . 2 ) dimension 23 . 0 21 . 2 11 . 0 13 . 0 13 . 0 23 . 0stability (%) odor ** none fnt fnt fnt fnt med______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint table 8______________________________________ comparative example 10 11 16 17 14 15______________________________________catalyst ( parts by weight ) * teda - l33 -- 0 . 95 0 . 40 0 . 40 -- -- toyocat - dt 1 . 10 0 . 55 0 . 30 0 . 30 -- -- tmdda -- -- -- -- -- -- tmdoda -- -- -- -- -- -- tmhmda -- -- 1 . 00 -- -- -- tmhdda -- -- -- 2 . 00 -- -- dmcha -- -- -- -- 2 . 40 -- mdcha -- -- -- -- -- 11 . 0reactivity ( seconds ) cream time 7 10 12 11 13 12gel time 50 50 50 49 50 50tack free time 61 63 63 65 73 75rise time 80 74 75 78 78 85foam propertiesfree density ( kg / m . sup . 3 ) 26 . 3 26 . 8 26 . 5 26 . 5 26 . 6 27 . 0mold density ( kg / m . sup . 3 ) overall 30 . 0 29 . 7 29 . 5 30 . 0 29 . 2 30 . 3core 28 . 7 28 . 0 27 . 9 28 . 4 27 . 6 28 . 4curing rate ( shore c ) 50 58 57 53 60 20adhesion strength 1 . 4 3 . 2 3 . 5 6 . 0 3 . 3 1 . 2 ( kg / 25 cm . sup . 2 ) dimension stability (%) 9 . 4 20 . 0 30 . 5 28 . 5 24 . 1 7 . 3odor ** med med strg fnt strg fnt______________________________________ * weight parts based on 100 parts by weight of polyol ** strg : strong , med : medium , fnt : faint