CN1153791A - Process for preparing polytetramethylene carbonate diol - Google Patents
Process for preparing polytetramethylene carbonate diol Download PDFInfo
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- CN1153791A CN1153791A CN 96112432 CN96112432A CN1153791A CN 1153791 A CN1153791 A CN 1153791A CN 96112432 CN96112432 CN 96112432 CN 96112432 A CN96112432 A CN 96112432A CN 1153791 A CN1153791 A CN 1153791A
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Abstract
The present invention discloses prodn process of polybutanediol carbonate. It features that in the presence of acid compound, 1,4-butanediol is reacted with carbonate selected from dialkyl carbonate, diaryl carbonate and alkylene carbonate. The said method can obtain high yield of polybutanediol carbonate with larger molecular weight even if in the high temp and other large-reaction speed conditions, and this is favourable for industrial-scale production. Selecting the prepolymer produced with the said polybutanediol carbonate and aliphatic diiso cyanate and elongating its chain with chain elongating agent can produce thermoplastic polyurethane with excellent light, hydrolysis, oil, acid and alcohol resistance.
Description
The present invention relates to the manufacture method of the novelty of polytetramethylene carbonate diol.In more detail, relate to a kind of manufacture method that technical scale is made polytetramethylene carbonate diol that helps, it is a kind of with photostabilization, oil resistant acidity, the anti-manufacture method that adds all good novel thermoplastic urethane of water decomposition, alcohol resistance aspect as the novelty of the poly-carbonic acid-butanediol ester of raw material manufacturing, it is characterized in that, in the presence of acidic substance, make 1,4-butyleneglycol and the carbonic ether that chooses from dialkyl carbonate, diaryl carbonate and alkylene carbonate react.The application of the invention method even under the big condition of speed of response such as high temperature, can suppress also to become that by product generates and molecule cuts off the side reaction of reason, the polytetramethylene carbonate diol that can have the molecules of interest amount with the high-level efficiency acquisition.
Though thermoplastic polyurethane has very high praise at aspects such as obdurability, oil-proofness, wearabilitys, and has enlarged its marketability, have still so far that photostabilization is not enough, life-time service can cause many problems such as flavescence.For example in the formed material purposes of urethane, in the high purposes such as watchband of timeliness n, this jaundice changes especially is a problem, and the variable color that causes in order not make this passage in time is too showy, generally be with black.And, in recent years, when urethane is used to do watchband is this with people's skin directly contacts product material, find that the sebum composition grease that contains sweat can cause the urethane deterioration, therefore, be used for the urethane of these purposes, its oil resistant ester is most important rerum natura.As the example of this based article, other also can enumerate bearing circle, speed control lever of auto parts etc.
And polyurethane coating is at the lamination synthetic leather.In the leather fields such as dipping combined artificial leather, the wearability of thermoplastic polyurethane, quality, outward appearance etc. all have higher rating, can be used for leather shoes, the various uses such as seat of suitcase, belt, gloves, sofa, automobile.Yet used urethane nearly all is polyester or polyethers urethane in these goods, thereby produces variety of problems.For example, furniture such as sofa or office chair, or seat cushions etc. directly contacts in the purposes of use with human body for a long time, owing to the water decomposition that adds of polyester urethane resin, make surface band viscosity, produce tackiness, this situation is in case significantly, will make the urethane resin layer deterioration, so that produce from phenomenons such as base material strip down, thereby ability life-time service not.Under the situation of polyethers urethane, though anti-to add water decomposition good, but not only the oil resistant ester is not enough, and as very important characteristic in this class purposes, promptly the patience of contained alcohol also is not enough in the hair care articles to the people, if life-time service, urethane tree resin layer deterioration so that not ability use.In order to solve this class problem, the someone advises using by 1,6-hexylene glycol deutero-polycarbonate ester class urethane (open clear 56-63079 communique referring to the spy of Japan, the spy of Japan opens clear 59-100778 communique, and the spy of Japan opens clear 59-100779 communique).
These are by 1, in the polycarbonate-based urethane of 6-hexylene glycol deutero-, as vulcabond, the urethane that the effect aromatic diisocyanate makes is in anti-water decomposition, the alcohol resistance of adding, aspects such as oil resistant ester increase than polyester urethane and polyethers urethane really, yet because its photostabilization is poor, in case life-time service is promptly can metachromatism remarkable, resin layer also can produce deterioration.On the other hand, as vulcabond, the urethane that uses aliphatic diisocyanate to make, though increase aspect the water decomposition in photostabilization, anti-adding, alcohol resistance, the acid aspect of oil resistant enough and needless to say, yet problem in the practicality is arranged, just wishing to solve.
On the other hand, about polycarbonate-based urethane, costing an arm and a leg of poly-carbonate diol ester is a big problem, generally when carrying out suitability for industrialized production, use commercially available 1, the 6-hexylene glycol replaces poly-carbonate diol ester, and old friends wish to have a kind of aspect of performance good, the poly-carbonate diol ester that price is also cheap.
In view of above-mentioned condition, present inventors are for overcoming the shortcoming of former thermoplastic polyurethane, carry out deep research, if unexpected discovery of result will be with 1, the number-average molecular weight that the 4-butyleneglycol makes as raw material is 500-10,000 polytetramethylene carbonate diol is as the carbonate diol ester, and when using aliphatic diisocyanate as organic diisocyanate, can obtain photostabilization.Anti-water decomposition, alcohol resistance and all good urethane of oil resistant acidity of adding.
About a spot of report once being arranged by polytetramethylene carbonate diol deutero-urethane, Polymer for example, Vol.33, No.7, reported urethane in the 1384-1390 page or leaf (1992) by polytetramethylene carbonate diol deutero-cross-linking type, yet in injection molding, insufficient formability in the purposes such as extrusion molding, and its viscosity is high-leveled and difficult with practicality in as the coating purposes, uses its stability that problem is also arranged as latex.On the other hand, about by polytetramethylene carbonate diol deutero-thermoplastic polyurethane, No. 710940, italian patent and Polymer (Korea S) Vol.14, No.5, the 487-496 page or leaf also has report, but all uses 4 in nineteen ninety, 4 '-'-diphenylmethane diisocyanate is as organic diisocyanate, and the inferior problem of photostabilization is all arranged.
About by as 1 of the polytetramethylene carbonate diol of one of raw material of thermoplastic polyurethane, the method that the 4-butyleneglycol is made, as the spy of Japan open the special public clear 63-12896 communique of clear 55-56124 communique and Japan disclosed, same with commercially available poly-carbonic acid hexyl diol ester, make 1, carbonic ethers such as 4-butyleneglycol and dialkyl carbonate, diaryl carbonate or alkylene carbonate carry out transesterification reaction, and this method is known.Yet, if react with these methods, carbonic ether and 1, the end of the low-molecular weight polymer of 4-butyleneglycol or generation reacts, can produce by product tetrahydrofuran (THF) (to call " THF " in the following text), so molecular weight is difficult to rise existing problems aspect productivity.Therefore, in order to prevent this side reaction, can take to reduce measures such as temperature of reaction, yet, under the situation that reduces temperature of reaction, again can the by-product butyl carbonate, molecular weight still is difficult to improve, therefore, from the viewpoint of boosting productivity, can not deal with problems, and because the THF of by-product makes the decompression reaction become difficult, and in order to make the concentration reduction that is discharged into the THF in the atmosphere by vacuum pump.Also need to be provided with in addition equipment such as absorption tower, thus technical scale advantageously to produce polytetramethylene carbonate diol be impossible.
Present inventors study the favourable manufacture method of technical scale as the raw material-polytetramethylene carbonate diol of thermoplastic polyurethane of the present invention, the result is surprised to find that, when in the presence of acidic cpd, carrying out above-mentioned transesterification reaction, can suppress side reaction significantly, make the yield of the bigger polytetramethylene carbonate diol of molecular weight good, help industrial-scale production.
The result of study that the present invention finishes with regard to being based on above-mentioned all opinions.
Therefore, the purpose of this invention is to provide the favourable manufacture method of technical scale as the raw material-polytetramethylene carbonate diol of all good novel thermoplastic urethane of a kind of photostabilization, hydrolytic resistance, alcohol resistance and oil resistant acidity.
Above-mentioned and other all purpose of the present invention, all features and all interests can more clearly understand by the following detailed description carried out referring to accompanying drawing and the narration in the appending claims.
Description of drawings:
Fig. 1 is the IR spectrogram of the polytetramethylene carbonate diol that made by embodiment 1.
Fig. 2 is that urethane that the poly-carbonic acid-butanediol ester, lipid acid vulcabond and the chain extension agent that make with the inventive method obtain is dissolved in organic solvent and the coating composition that forms is coated in synthetic leather with on the base material, and the longitdinal cross-section diagram of the dry lamination synthetic leather (being made by embodiment 12) that becomes epidermal area and make.
The invention provides raw material as thermoplastic polyurethane of the present invention-be the favourable manufacture method of technical scale of the polytetramethylene carbonate diol of following formula (1) expression, the feature of this method is, having in the presence of the acidic cpd, make 1,4-butyleneglycol and from dialkyl carbonate, the carbonate reaction that chooses in diaryl carbonate and the alkylene carbonate;
(P is the number with mean value of 3-85 in the formula).
The polytetramethylene carbonate diol that makes with technical scale by the inventive method, the prepolymer (A) that particularly reacts and obtain with aliphatic diisocyanate, (B) carries out chain extension by the chain extension agent, just can obtain to can be used as coating, tackiness agent, latex, moulding product material etc., photostabilization, oil resistant acidity, hydrolytic resistance, novel thermoplastic urethane that alcohol resistance is all good.
That is,, can provide a kind of thermoplastic polyurethane according to the present invention, it be the prepolymer (A) that is expressed from the next derive the prepolymer composition that obtains and by chain extension agent (B) derive and chain extension agent composition constitute:
(in the formula, X is
, wherein, m is the number with mean value of 3-85;
Y is the residue of aliphatic diisocyanate;
N is the number with mean value of 1-50),
Prepolymer composition (A) is to be 500-10 by number-average molecular weight, and 000 polytetramethylene carbonate diol composition (1) and aliphatic diisocyanate composition (2) constitute;
Chain extension agent (B) is to be that glycol, molecular weight below 300 is the chain extension agent with reactive hydrogen that chooses diamines, hydrazine and the water below 300 from molecular weight;
This prepolymer (A) makes chain extension by this chain extension agent (B).
The number-average molecular weight of used polytetramethylene carbonate diol is 500-10 during preparation prepolymer (A), 000, be preferably 800-5,000.
As aliphatic diisocyanate, can use straight chain, any in side chain and the cyclic type, but preferably the carbonatoms in fatty group is 4-13.Aliphatic diisocyanate as straight chain, can exemplify: two isocyanic acid Aden esters, the inferior pentyl ester of two isocyanic acids, the inferior own ester of two isocyanic acids, the inferior monooctyl ester of two isocyanic acids etc., as the cyclic aliphatic diisocyanate, can exemplify: 1-methyl cyclohexylidene-2,4-vulcabond (hydrogenation TDI), 1,2-dimethyl cyclohexylidene-ω, ω '-vulcabond (hydrogenation-XDI), isophorone diisocyanate (IPDI), dicyclohexyl methylene radical-4,4 '-vulcabond (hydrogenation MDI) etc.
The thing that should note of associated therewith, when adopting aromatic diisocyanate to replace above-mentioned aliphatic diisocyanate, shown in the comparative example 5-6 described as follows, photostabilization significantly degenerates, and variable color and physical strength be variation also, can not be for practical.
Prepolymer (A) shown in (A), is to be made of tetramethylene carbonic ether composition, amino-formate bond and vulcabond composition, and two ends have the non-crosslinked type straight chain shape prepolymer of isocyanate group, demonstrate thermoplasticity.In formula (A), m and n value can suitably be selected according to the number-average molecular weight (30,000-200,000) of target thermoplastic urethane.
As chain extension agent (B), can use and be selected from molecular weight is that glycol, molecular weight below 300 is the chain extension agent of diamines, hydrazine and water below 300.Specifically can exemplify: ethylene glycol, 1, the 4-butyleneglycol, 1,5-pentanediol, neopentyl glycol, 1, glycolss such as 6-hexylene glycol, quadrol, propylene diamine, hexamethylene-diamine, tolylene diamine, xylylene diamines, diphenyl diamine, diaminodiphenyl-methane, diamino cyclohexyl-methane, two amines, hydrazine and water etc. such as piperazine, 2-methylpiperazine, isophorone diamine.
Owing to used this chain extension agent (B), above-mentioned thermoplastic polyurethane is non-crosslinked and demonstrates thermoplastically, can carry out forming process at an easy rate, and is very stable when using as coating composition, demonstrates good coating property.Shown in comparative example 11 described later, as the chain extension agent, if when adopting the bridging property trivalent alcohol without specific chains used among the present invention prolongs agent (B), reaction soln and viscosity sharply rise in the chain extension reaction, thereby can not get stable coating composition.
Chain extension agent (B) is to the ratio of prepolymer (A), can carry out appropriate selection according to the number-average molecular weight of the thermoplastic polyurethane of target, but in general, the reactive hydrogen of chain extension agent (B) to the mol ratio of the NCO of prepolymer (A) with 2-0.5 (but except 1) for well, be preferably 1.2-8 (but except 1).
Manufacture method as above-mentioned thermoplastic polyurethane, can adopt the known technology of urethane reaction aspect, for example by making the reaction of polytetramethylene carbonate diol and aliphatic diisocyanate, the carbamate prepolymer (A) of NCO end is synthetic, add chain extension agent (B) therein, making it the prepolymer method that polymer quantizes to obtain the thermoplastic polyurethane of target is exactly a kind of advantageous method.
In the building-up reactions of this thermoplastic polyurethane, also can use used known polymerizing catalyst in the urethane reaction of organic metal salt etc. of an amount of tertiary amine and tin, titanium as required.For example, can use the various polymerizing catalysts of controlling record in work " polyurethanes technology " (Japan, Nikkan Kogyo Shimbun's publication) the 23-32 page or leaf (1976) at rock Tian Jing.
The building-up reactions of thermoplastic polyurethane also can be used aliphatic diisocyanate is the inert solvent carries out.For example can be separately or mix more than two kinds and use with dimethyl formamide, diethylformamide, methyl-sulphoxide, N,N-DIMETHYLACETAMIDE, tetrahydrofuran (THF), methyl iso-butyl ketone (MIBK), diox, pimelinketone, benzene, toluene equal solvent.
In the building-up reactions of thermoplastic polyurethane, also can add end-capping reagent as required and block end.As end-capping reagent, can exemplify: lower aliphatic monohydroxy-alcohols such as methyl alcohol, ethanol; Or carbonatoms such as ethamine, Isopropylamine, diethylamine, 2-DEHA is alkylamine about 2-12 etc.
Other manufacture method as above-mentioned thermoplastic polyurethane, can also be to use solvent that prepolymer (A) is synthetic, add chain extension agent (B) after being dispersed in this prepolymer (A) emulsification in the water and make it the polymer quantification, remove solvent subsequently, make thermoplastic polyurethane with the latex state.
The number-average molecular weight of above-mentioned thermoplastic polyurethane is 30,000-200, and 000, be preferably 40,000-100,000.If number-average molecular weight is lower than 30,000, the photostabilization of the thermoplastic polyurethane that then makes and mechanical characteristics are good inadequately, for example, resemble shown in the comparative example 4 described later the photostabilization extreme difference.On the other hand, if surpass 200,000, processibility variation then, shown in the comparative example 10, coating composition viscosity significantly raises as described later, can't be for practical.
The gel content of above-mentioned thermoplastic polyurethane is 5 (weight) below the %, in fact preferably 0 (weight) %.The content of gel is in case above 5 (weight) %, and processibility degenerates, can't be for practical.And, since poorly soluble to solvent, the coating composition that can not obtain having stable viscosity.
That is to say that above-mentioned thermoplastic polyurethane is the prepolymer (A) and chain extension agent (B) reaction that following formula is represented basically, by this chain extension agent (B) chain extension of this prepolymer (A) is made;
(in the formula, X is
, wherein, m is the number with mean value of 3-85;
Y is the residue of aliphatic diisocyanate;
N is the number with mean value of 1-50),
Prepolymer composition (A) is to be 500-10 by number-average molecular weight, and 000 polytetramethylene carbonate diol composition (1) and aliphatics diisocyanate resin composition (2) constitute;
Chain extension agent (B) is to be that glycol, molecular weight below 300 is the material with reactive hydrogen that chooses diamines, hydrazine and the water below 300 from molecular weight;
The material that makes has 30,000-200, and 000 number-average molecular weight, and wherein the content of gel is below 5 weight %, and it is actually a kind of uniform material.
As one of purposes of above-mentioned thermoplastic polyurethane, this urethane is dissolved in its organic solvent and the coating composition that forms.
Aforementioned coating composition, can also use above-mentioned aliphatic diisocyanate is the inert solvent with the directly use of the synthetic back of thermoplastic polyurethane of the present invention, but, also can further add ethanol, butanols, Virahol class (for example referring to the special public clear 63-29687 communique of Japan) in order to adjust purposes such as viscosity and control drying property.
For thermotolerance, the photostabilization of above-mentioned thermoplastic polyurethane and coating composition, purposes such as processibility also can further be used various known additives.As these additives, can exemplify: oxidation inhibitors such as phenols oxidation inhibitor, amine oxidation inhibitor, sulphur class oxidation inhibitor, Phosphorus oxidation inhibitor, or the UV light absorber of benzophenone, salicylate class, benzotriazole category, metal complex class, ヒ Application ダ-ト ァ シ Application class, and reinforcing fiber, weighting agent, tinting material, glued membrane agent, fire retardant etc. (for example open flat 3-11141 communique (corresponding to DE.P39309995.9) referring to the spy of Japan, special public clear 53-30760 communique of Japan and spy open clear 57-117523 communique).
Another purposes as above-mentioned thermoplastic polyurethane also can provide the lamination synthetic leather, and this leather is to be attached to directly or indirectly on the above-mentioned thermoplastic polyurethane with film like on the one side at least of fibrous substrate and to constitute.
Above-mentioned lamination synthetic leather as shown in Figure 2, is that aforementioned coating composition is coated on the fibrous substrate (hereinafter to be referred as " base material ") that synthetic leather uses, and the dry back of backbone is formed epidermal area and makes.
As fibrous substrate, can exemplify: natural fibers such as cellulosic fibre, regenerated fibre; Independent or the two or more cloths that make of synthon such as polyester, nylon, vinylon, acrylic fibers.
Above-mentioned lamination synthetic leather can be with known the whole bag of tricks manufacturing.For example, at least one surface of base material, directly apply coating composition, or the middle layer of foaming carbamate layer is set on base material, the middle layer perhaps is not set, but the formation adhesive linkage applies coating composition indirectly by it, removes then and desolvates.Can also form coating composition film of the present invention earlier, by tackiness agent it is fitted on the base material then; Form the epithelium that constitutes by coating composition thereby coating composition can also be coated on the mold release film, by tack coat this film surface is fitted in base material after, make the lamination synthetic leather thereby again mold release film is peeled off.In the aforesaid method, be best with the method that adopts mold release film.
The tackiness agent that uses during the lamination synthetic leather is made, for example can use aforementioned coating composition itself, also can adopt other coating composition that constitutes by other urethane resin, can also adopt the material that in these coating compositions, is mixed with stiffening agents such as polymeric polyisocyanate.
As adhesive method, can be behind application of adhesive on the epithelium of base material or coating composition of the present invention, again base material and epithelium are fit together, solvent evaporates is fallen; Also can be on base material and epithelium application of adhesive all, treat solvent evaporates after, make base material and epithelium press knot to be in the same place.
Mold release film as using can exemplify: silicon class mold release film, polypropylene-base mold release film, polyester mold release film etc.
Dipping combined artificial leather also can be provided, this leather is in the many interfibrous gap of fiber base material, make above-mentioned thermoplastic polyurethane be even shape basically and be present in wherein, thereby this gap of filling is synthesized together these fibers simultaneously and constitutes dipping combined artificial leather.
Dipping combined artificial leather, not as above-mentioned lamination synthetic leather, to apply with thermoplastic polyurethane on the surface of fiber base material, but use the coating composition impregnation of fibers matter base material that thermoplastic polyurethane is dissolved in its organic solvent and forms, make as the solids fraction thermoplastic polyurethane that includes in the coating composition and remain in the fibrous substrate, in the many interfibrous gap of fibrous substrate, thermoplastic polyurethane is uniform state substantially and exists, and constitutes dipping combined artificial leather thereby these fibers are combined this gap of filling the time.
As the fibrous substrate of dipping combined artificial leather, for example, can adopt the non-woven fabrics (to call the fluffing non-woven fabrics in the following text) that makes wildness.As this nappy non-woven fabrics, can adopt the superfine fiber that only will form fluffing part to mix and knit the mixed sheet of knitting that forms, or mix with superfine fibre with as the cloth of supporting material or the coarctate material of tissue layer and to knit the mixed sheet etc. of knitting that forms.
The material of superfine fibre, staple lengths etc. can be selected arbitrarily, but for the fine and close or bright effect of the flap surface grade that obtains matte style and ヌ バ ッ Network style, the fineness of this superfine fibre is preferably below 0.5 dawn.As the superfine fibre material, preferably polyester, polymeric amide, polyacrylonitrile, Mierocrystalline cellulose, copper ammonia fibres etc. are preferred yet contain the material that can be partly dissolved polyvinyl alcohol (PVA) fiber of removing when aftertreatment.As staple length, can be cut into the staple fibre shape of 1-50mm, also can be that 100mm is above or be the macrofiber shape basically, treat with a certain discrimination according to purposes.As the manufacture method of this superfine fibre, available known method, for example, sea-island fibre method, blend fiber method, direct spinning, molten stream method, spun-bond process etc.
On the other hand, the cloth as the supporting material of above-mentioned superfine fibre can use cloths such as horizontal knitmesh, warp-knitted fabric, have the fabric of tissue such as plain weave.Constitute the former yarn of these fabrics, straight yarn preferably, false twist processing yarn etc.
Dipping combined artificial leather can be with various known method manufacturings.For example, at first by weber's method and broadwise carding machine at random or copy after the slurry method forms non-woven fabrics with superfine fibre (the PVA fiber that solubilized was removed when it partly contained above-mentioned aftertreatment), by pin punching or high-voltage column-like water stream etc. superfine fibre is mixed again and make it to become one, obtain mixing sheet by the fluffing that superfine fibre constitutes.Or after forming the non-woven fabrics that constitutes by superfine fibre, will compile thing and/or fabric and insert after the central lamination, make superfine fibre and compile thing and/or fabric mixes mutually, thereby obtain mixing sheet by the fluffing that superfine fibre and volume thing and/or fabric constitute.
Then, in order to protect the fluffing part, apply carboxymethyl cellulose (CMC) aqueous solution on the sheet in these nappy mixing; be immersed in the coating composition then; extract and remove fluffing subsequently and mix PVA fiber and CMC in the sheet,, obtain dipping combined artificial leather through super-dry.
Method of the present invention, be a kind of raw material of thermoplastic polyurethane as mentioned above---be the favourable manufacture method of technical scale of the poly-carbonic acid-butanediol ester of following formula (1) expression, the feature of this method is, having in the presence of the acidic cpd, make 1,4-butyleneglycol and from dialkyl carbonate, the carbonate reaction that chooses in diaryl carbonate and the alkylene carbonate;
(P is the number with mean value of 3-85 in the formula)
As the dialkyl carbonate of carbonic ether, can exemplify methylcarbonate, diethyl carbonate and dibutyl carbonate etc.; As diaryl carbonate, can exemplify diphenyl carbonate and carbonic acid dinaphthyl ester etc.; As alkylene carbonate, can exemplify ethylene carbonate, Texacar PC etc.These carbonic ethers can use separately or be used in combination more than 2 kinds.
In addition, 1, the ratio of 4-butyleneglycol and carbonic acid is expressed as 10 with mol ratio usually: 1-1: 10, preferably 1: 2-2: select in 1 the scope.
The building-up reactions of polytetramethylene carbonate diol is for example shown in following formula (2), (2 ').
Or
In above-mentioned formula (2) or (2 '), X and Y are respectively alkoxyl group or phenoxy group, X and Y can be identical also can be inequality.Each constant of stoichiometry regulation naturally of a, b, c, d and e, p is the number with mean value of 3-85, q is an integer.
This reaction is 1, the transesterification reaction of 4-butyleneglycol and carbonic ether, and be balanced reaction, thereby react by in reaction system, removing secondary alcohols of giving birth to.As the by product of this reaction, tetrahydrofuran (THF) (THF) is arranged and as 1, the cyclic carbonate of 4-butyleneglycol is a carbonic acid butylidene ester (BC).Its formation mechanism, can think has following 2 routes.That is, route 1 shown in (3), (3 '), is by from 1, thereby the direct decarboxylation of 4-butyleneglycol and carbonic ether and direct cyclisation produce into the route of THF and BC, and 1, the initial reaction stage the when concentration of 4-butyleneglycol or carbonic ether is high plays dominating role.
Or
In above-mentioned formula (3) or (3 '), X and Y are respectively alkoxyl group and phenoxy group, X and Y can be identical also can be inequality.Each constant of stoichiometry regulation naturally of a, b, c, d and e, q is an integer.
On the other hand, as the route 2 of another route, shown in following (4) formula, be by 1, the end of the polytetramethylene carbonate diol that 4-butyleneglycol and carbonic ether generate, cyclisation and cyclisation decarboxylation and the route that generates in the high reaction later stage of polymer concentration, plays domination and uses.
In the formula (4), p is the integer with mean value of 3-85.
As shown in above-mentioned formula (3), (3 ') and (4), in the building-up reactions of polytetramethylene carbonate diol, owing to making speed of response, side reaction reduces during initial reaction stage, in the reaction later stage, the end of polymkeric substance (polytetramethylene carbonate diol) is owing to side reaction is cut off, thereby molecular weight is difficult to raise, and it is very difficult generating polytetramethylene carbonate diol expeditiously.
As the reason of these side reactions, details is also not clear, but can think owing to common thermolysis, and the decomposition that the trace metal that exists in the reaction system causes, the decomposition that micro-alkali causes, catalysts promotion decomposition etc. are caused.In order to suppress these side reactions, considered to take the method that reduces the method for temperature of reaction and do not use catalyzer etc., but brought speed of response to reduce, thereby be disadvantageous; Also consider to remove the method for trace ingredients on the other hand, if but consider that side reaction is a pyrolysis, just can not suppress by product fully.
Yet, as described later shown in embodiment 1-6 and the comparative example 1-3, if interpolation acidic cpd, though unclear mechanism wherein, but be surprised to find that, side reaction when not only having suppressed high temperature, especially fully suppressed the route shown in the above-mentioned formula (4), and the growing amount of THF significantly reduces, number-average molecular weight is 500-10,000 (in the above-mentioned formula (1), corresponding to the material of p=3-85), 500-5 preferably, 000 polytetramethylene carbonate diol just can high yield, and the technical scale utmost point advantageously makes.
The manufacture method of polytetramethylene carbonate diol of the present invention can exemplify out as shown in above-mentioned formula (2) or (2 '), is in the presence of acidic cpd, makes 1, and 4-butyleneglycol and carbonic ether carry out the method for transesterify; Or as shown in following (5) or (5 '), 1,4-butyleneglycol and carbonic ether exchange, with number-average molecular weight is that lower molecular weight polytetramethylene carbonate diol about 300-1000 is synthetic, yet after removing unreacted monomer, add carbonic ether again, in the presence of acidic cpd, carry out the method for chain extension reaction;
Or
In above-mentioned formula (5) or the formula (5 '), X and Y are respectively alkoxyl group and phenoxy group, and X also can be identical with Y.A, b, c, d and e each naturally the constant γ of stoichiometry regulation be number with mean value of 2-8, p is the number with mean value of 3-85, q is an integer.
Also have, as shown in following (6) or (6 '), in the presence of acidic cpd with the method for the own condensation of low-molecular-weight polytetramethylene carbonate diol.
Or
In above-mentioned formula (6) or the formula (6 '), X and Y are respectively alkoxyl group or phenoxy group, X and Y also can be identical also can be inequality.Each constant of stoichiometry regulation naturally of a, b, c, d and e, γ is the number with mean value of 2-8, and p is the number with mean value of 3-85, and q is an integer.
Can adopt above-mentioned any method.But, in any method, this condition of reacting in the presence of acidic cpd all is important.
In the synthetic reaction of polytetramethylene carbonate diol,, distillation tower preferably is installed on reactor is reacted for the alcohols that pair is given birth to selectively is rejected to outside the system.
And different, preferably, 1, the remaining many initial reaction stage of 4-butyleneglycol are in order to suppress side reaction, common suitable selection between 80 ℃-200 ℃ according to reaction method for temperature of reaction; In the reaction later stage that polymer concentration increases, preferably between 120 ℃-250 ℃, suitably select.
As for reaction pressure,, can in normal pressure-13.3Pa (0.1mmHg) scope, suitably select in order to remove secondary alcohols of giving birth to effectively.
Reaction formation can be an intermittent type, semibatch, any in the continous way.
The acidic cpd that uses in the present invention in order to prepare poly-carbonic acid butanediol fat, preferably: phosphoric acid, phosphorous acid, acid phosphoric acid ester, phosphorous acid ester, phosphoric acid ester.Specifically can exemplify: acid phosphoric acid esters such as phosphoric acid, phosphorous acid, methyl orthophosphoric acid, dimethyl phosphate, phosphide ethyl ester, diethyl phosphoric acid, phosphoric acid propyl ester, di(2-ethylhexyl)phosphate propyl ester, p isopropylbenzoic acid ester, diisopropyl phosphate, butyl phosphate, dibutyl phosphate, phosphoric acid dodecane ester, the two dodecane esters of phosphoric acid, phosphoric acid octadecane ester, the two octadecane esters of phosphoric acid, phosphoric acid ten benzyl esters, dioctylphosphoric acid ester, di(2-ethylhexyl)phosphate oleic acid ester, diphenyl phosphate; Phosphorous acid-methyl esters, phosphorous acid esters such as dimethylphosphite, phosphorous acid (2-ethylhexyl) ester, phosphorous acid two (2-ethylhexyl) ester, phosphorous acid (dodecylphenyl) ester, phosphoric acid ester such as benzyl phosphate ester, phosphoric acid di-n-butyl, the two n-Hexadecane esters of phosphoric acid, phosphoric acid didecyl ester, di(2-ethylhexyl)phosphate (2-ethylhexyl) ester, di(2-ethylhexyl)phosphate n-hexyl decyl ester, diphenyl phosphate.
The addition of acidic cpd generally is equivalent to the total amount (for example in the method for formula (2) or (2 ') expression, 1, the total weight of the carbonic ether of 4-butyleneglycol) of charging feedstock, its consumption 1ppm-10, and 000ppm is preferably in the scope of 5-500ppm.If the addition of these acidic cpds surpasses 10,000ppm then hinders reaction; If not enough 1ppm then can not reach the effect that suppresses side reaction.
As the addition means of acidic cpd, both can disposable interpolation in reaction, also can add continuously.Acidic cpd can be in reaction any stage add, but in general, in that the high reaction of the sort of polymer concentration of above-mentioned formula (5) expression mid-term-it then is the most effective that the later stage adds.
In the building-up reactions of polytetramethylene carbonate diol,, and use catalyzer also can react even catalyst-free also can react.As catalyzer, (for example can use known transesterification catalyst, can reference: USP4440937, USP3426042, USP3663569, the spy of Japan open clear 55-56124 communique and the spy of Japan opens clear 62-501080 communique), for example, lead acetate, zinc oxide, diethoxy lead, lead compounds such as dipropoxy lead, four titanium propanolates, titanium compounds such as four titanium butoxide, metals such as sodium, potassium, lithium, rubidium, caesium, magnesium, calcium, strontium, barium, aluminium, cobalt, germanium, cerium, manganese, antimony, tin, zinc, the salt of these metals, oxide compound, title complex, metal alkoxides etc.
The addition of catalyzer, generally with respect to 1, the total weight of 4-butyleneglycol and carbonic ether is 1ppm-1,000ppm preferably uses in the 5-500ppm scope.
Poly-carbonic acid-the butanediol ester that so makes not only can be used as the manufacturing raw material of the present invention's thermoplastic polyurethane, but also can use in purposes such as the soft chain segment of thermoplastic elastomer, polymeric plasticizer.
Below enumerate embodiment, the present invention is described in further detail, but the present invention is not limited to these embodiment." part " among the embodiment unless other special stipulation are arranged, all refers to " weight part " in this article.
The rerum natura of the thermoplastic polyurethane among the embodiment is estimated in order to following method.
(1) photostabilization
With the meter that fades (Japan, ス ガ trier society system), thermoplastic polyurethane test portion (wide 10mm, long 60mm, thick 100 μ m) carried out in 63 ℃ 100 hours exposure test.Take out test portion then, measure xanthochromia degree (△ E value), simultaneously, under the following conditions, measure, obtain the film toughness conservation rate by following formula then according to JIS K-7311 with color colour-difference meter (CR-200, Japan, ミ ノ Le society system).
Mensuration machine: テ Application シ ロ Application tensile testing machine (RTA-100, Japan, ォ リ ェ Application テ ッ Network society system)
Length: 30mm nips
Draw speed: 300mm/ branch
Measure atmosphere: 25 ℃, 65% relative humidity (RH)
(2) oil resistant acidity:
Thermoplastic polyurethane test portion (wide 10mm, long 60mm, thick 100 μ m) is placed in the oleic acid after room temperature flooded for 1 week, obtains swelling capacity and film toughness conservation rate by following formula.
The film toughness conservation rate be with above-mentioned (1) photostabilization situation under under the same terms, measure according to JIS K-7311.
(3) alcohol resistance
With thermoplastic polyurethane test portion (wide 10mm, long 60mm, thick 100 μ m), in ethanol under the room temperature after 1 week of dipping, the same terms mensuration down in the acid situation of above-mentioned (2) oil resistant, and obtain swelling capacity and the strong conservation rate of film by same formula.
(4) anti-ly add water decomposition
Thermoplastic polyurethane test portion (wide 10mm, long 60mm, thick 100 μ m) flooded 7 days in 100 ℃ of hot water after,, obtain the molecular weight conservation rate by following formula with gel permeation chromatograph (GPC) determining molecular weight.
(5) number-average molecular weight of thermoplastic polyurethane:
Make dimethyl formamide (DMF) 1 (weight) the % solution of thermoplastic polyurethane, use GPC, obtain the number-average molecular weight (polystyrene standard conversion) of thermoplastic polyurethane under the following conditions.
Pillar: Shodex KD-804ey DD805 (2 series connection), Japan, clear and electrician society system
Post baking oven: CTO-6A
Japan, Shimadzu Seisakusho Ltd.'s system
Temperature: 40 ℃
Flow velocity: 1ml/ minute
Detector: differential refractometer (RID-6A, Japan, society of Shimadzu Seisakusho Ltd. system)
Data processing equipment: CP-8000, Japan, eastern ソ-society's system
(6) gel content of thermoplastic polyurethane:
Thermoplastic polyurethane 10g is put into the Erlenmeyer flask of 200ml, add DMF90g, vibration is 60 minutes in the vibrator of temperature adjustment to 50 ℃.Then,, leach not dissolved constituent, this not after the dissolved constituent drying, is measured its weight, obtain gel content by following formula with 400 purpose screen filtrations.
The weight (g)/10 (g) * 100 of gel content (weight %)=not dissolved constituent
Embodiment 1
Operation (1)
Be provided with stirrer, in 3 liters of reactors of thermometer and fractionating tube, the ethylene carbonate 1584g that packs into (18 moles), 1,4-butyleneglycol 1440g (16 moles) and lead acetate 3mg are 130 ℃ in temperature, and pressure is to make it to react 10 hours under 2.27KPa (17mmHg)-4.67KPa (35mmHg).At this moment, the cat head from separation column distillates the ethylene glycol of giving birth to as the unreacted carbonic acid ethyl and the pair of azeotropic component.In cold-trap, also find, with respect to pack into 1,4-ethylene glycol is that the tetrahydrofuran (THF) (to call in the following text: " THF ") of 2 moles of % generates.
Operation (2)
Then, pressure recovery to normal pressure, behind the interpolation ethylene carbonate 317g (3.6 moles), is risen to 150 ℃ with temperature, under pressure 2.27KPa (17mmHg)-4.67KPa (35mmHg), make it to react 8 hours.At this moment, the top from separation column distillates as azeotropic component unreacted carbonic acid ethyl and secondary ethylene glycol of giving birth to.In cold-trap, find to have with respect to pack into 1,4-ethylene glycol is that the THF of 2 moles of % generates.At this moment, there is the 1800g polytetramethylene carbonate diol to generate in the reactor, measures the result of its number-average molecular weight with GPC, be about 1500 (hydroxyl value=77.3mgKOH/g).
Operation (3)
Then, use pressure is fixed on normal pressure,, add di(2-ethylhexyl)phosphate (2-ethylhexyl) ester 0.1g, take out fractionating tube as acidic cpd, directly exhaust, then temperature being decided to be 150 ℃ of pressure is that 800Pa (6mmHg) is through separating the monomer of reaction in 1 hour.
Operation (4)
Then, temperature is decided to be 190 ℃, pressure is decided to be 533Pa (4mmHg), distillates 1, makes it to react 5 hours in the time of the 4-butyleneglycol, (the polytetramethylene carbonate diol 1740g of hydroxyl value=54.6mgKOH/g) that obtains number-average molecular weight and be 2050.At this moment, the by-product THF of generation, with respect to pack into 1, the 4-butyleneglycol is 1 mole of %.The by-product THF total amount of initial reaction stage, with respect to 1, the 4-butyleneglycol is 5 moles of %.The IR spectrogram of the polytetramethylene carbonate diol that generates is shown among Fig. 1.
Comparative example 1
Except do not add di(2-ethylhexyl)phosphate (2-ethylhexyl) ester in operation (3), all the other are all identical with embodiment 1, synthetic polytetramethylene carbonate diol.
The THF of by-product in operation (1), with respect to pack into 1, the 4-butyleneglycol is 2 moles of %.
In operation (2), generate polytetramethylene carbonate diol 1820g, (hydroxyl value=80mgKOH/g) that its number-average molecular weight is 1450.And, the THF of by-product, with respect to pack into 1, the 4-butyleneglycol is 4 moles of %.
Then, in operation (3), as mentioned above, do not add di(2-ethylhexyl)phosphate (2-ethylhexyl) ester, take out fractionating tube, isolate unreacted monomer.
Thereafter, in operation (4), be that 533Pa (4mmHg), temperature are to react under 190 ℃ at pressure, but the THF of by-product the decompression degree can not be lowered from 800Pa (6mmHg), thereby under the condition of 800Pa (6mmHg), distillating 1, reaction is 10 hours in the time of 4-two butanols.The THF of by-product, when monomer separation with respect to pack into 1, the 4-butyleneglycol is 4 moles of %, is 8 moles of % when butyleneglycol distillates.(the polytetramethylene carbonate diol 1530g of hydroxyl value=77.3mgKOH/g) that obtains number-average molecular weight and be 1500.Further continue reaction, but the decomposition of polymkeric substance becomes sharply, thereby the polymer quantification is had any problem.From the by-product THF total amount of initial reaction stage, with respect to pack into 1, the 4-butyleneglycol is 16 moles of %.
Embodiment 2
Except adding di(2-ethylhexyl)phosphate (2-ethylhexyl) ester 0.5g (embodiment 15 times), all the other are all identical with embodiment 1, fractionate out the unreacted carbonic acid ethyl and the by-product ethylene glycol of azeotropic component from the cat head of fractionating tube, reclaim THF with cold-trap.In reactor, generate number-average molecular weight and be 1480 polytetramethylene carbonate diol 1800g, the THF of by-product with respect to pack into 1, the 4-butyleneglycol is 4 moles of %.
Then, take out fractionating tube, directly exhaust, then pressure be under the 800Pa (6mmHg) through 1 hour after the unreacted monomer of separation.Be that 533Pa (4mmHg), temperature are to distillate 1 under 190 ℃ at pressure then, 4-butyleneglycol and reacting simultaneously 5 hours, (the polytetramethylene carbonate diol 1710g of hydroxyl value=52.1mgKOH/g) that obtains number-average molecular weight and be 2150.At this moment, the THF of generation, with respect to pack into 1, the 4-butyleneglycol is 4 moles of %.From the by-product THF total amount of initial reaction stage with respect to pack into 1, the 4-butyleneglycol is 4.4 moles of %.
Embodiment 3
Except reacting latter half of monomer separation condition is pressure 400Pa (3mmHg), outside 200 ℃ of temperature, 10 hours reaction times, uses the method identical with embodiment 1 to react.Its result, (the polytetramethylene carbonate diol 1500g of hydroxyl value=32mgKOH/g) that obtains number-average molecular weight and be 3500.At this moment, the THF total amount of by-product with respect to pack into 1, the 4-butyleneglycol is 5.5 moles of %.
Embodiment 4
Except use di(2-ethylhexyl)phosphate n-hexadecyl ester as acidic cpd, use the method identical to react with embodiment 1.Its result, (the polytetramethylene carbonate diol 1700g of hydroxyl value=58.9mgKOH/g) that obtains number-average molecular weight and be 1900.At this moment, by-product THF total amount with respect to pack into 1, the 4-butyleneglycol is 4.8 moles of %.
Embodiment 5
Except using the phosphorous acid 0.2g, use the method identical to react with embodiment 1 as acidic cpd.Its result, (the polytetramethylene carbonate diol 1730g of hydroxyl value=58.0mgKOH/g) that obtains number-average molecular weight and be 2000.At this moment, by-product THF total amount with respect to pack into 1, the 4-butyleneglycol is 4.9 moles of %.
Embodiment 6
The number-average molecular weight that will make with the method for comparative example 1 is the eggplant type flask that 1500 polytetramethylene carbonate diol 200g puts into 500ml, as acidic cpd, add the 10mg of di(2-ethylhexyl)phosphate (2-ethylhexyl) ester, 190 ℃ of temperature, distillate 1 through 2 hours limits under the pressure 400Pa (3mmHg), the 4-butyleneglycol reacts simultaneously.Generate the polytetramethylene carbonate diol of 190g, (hydroxyl value=46.4mgKOH/g) that its number-average molecular weight is 2500.
Comparative example 2
Except not adding di(2-ethylhexyl)phosphate (2-ethylhexyl) ester, use the method identical to react with embodiment 6, its result, by-product THF5g, number-average molecular weight is not seen increase.
Comparative example 3
Except not adding di(2-ethylhexyl)phosphate (2-ethylhexyl) ester, and reaction conditions is 200 ℃ of temperature, pressure 267Pa (2mmHg), outside 10 hours, uses with embodiment 6 same procedure and react.Its result generates THF10g, does not see that number-average molecular weight has increase.
Embodiment 7
205 parts of the polytetramethylene carbonate diols that embodiment 1 is made, the inferior own ester of two isocyanic acids is packed into for 100.8 parts and is had whipping appts, temperature is taken into account in the reactor of cooling tube, in 100 ℃ of reactions 4 hours, obtain the prepolymer of NCO end, in this prepolymer, add as 1 of chain extension agent, 44.63 parts of 4-butyleneglycols, as 0.60 part of the propyl carbinol of end-capping reagent, and as 0.007 part of two fourth tin dilaurate of catalyzer, (LABO is with omnipotent extrusion machine KR-35 type with omnipotent extrusion machine with interior laboratory of establishing kneader, Japan, large bamboo hat with a conical crown and broad brim pine chemical institute society), obtain urethane 170 ℃ of reactions after 2 hours.Then this urethane is extruded with screw extrusion press and formed sub-thread material bar, on tablets press, make pill.The number-average molecular weight of the polyurethane particles that makes is 85,000, and gel content is 0 (weight) %.Use this polyurethane particles, on pressure forming machine, make the plate that thickness is 100 μ m, make test film, measure photostabilization by this plate.It the results are shown in table 1.
Embodiment 8
205 parts of polytetramethylene carbonate diols, dicyclohexyl methyl hydride-4 that embodiment 1 is made, 4,52.4 parts of-vulcabond (hydrogenation MDI) and dibutyltin dilaurate are packed into for 0.013 part and are had in the reactor of whipping appts, thermometer and cooling tube, in 120 ℃ of reactions 4 hours, obtain the prepolymer of NCO end.In this prepolymer, add as 1 of chain extension agent, 8.15 parts of 4-butyleneglycols and as 15 parts of the propyl carbinols of reaction terminating agent, with interior laboratory of establishing kneader with omnipotent extrusion machine (LABO with omnipotent extrusion machine KR-35 type, Japan, large bamboo hat with a conical crown and broad brim pine chemical institute society system), 170 ℃ of reactions in the time of 3 hours down.Subsequently, screw extrusion press is made pill after forming sub-thread material bar on tablets press.The number-average molecular weight of the polyurethane particles that makes is 80,000, and gel content is 0 (weight) %.Use this polyurethane particles, make the plate that thickness is 100 μ m on pressure forming machine, make test film by this plate, measure photostabilization, it the results are shown in table 1.
Embodiment 9
Except using 1,44.21 parts of 4-butyleneglycols, and use propyl carbinol 1.28 especially, and other are all identical with embodiment 7, and making number-average molecular weight is 40,000, and gel content is the polyurethane particles of 0 (weight) %.Use this polyurethane particles, on pressure forming machine, make the plate that thickness is 100 μ m, make test film, measure photostabilization by this plate.It the results are shown in table 1.
Comparative example 4
Except using 1,43.42 parts of 4-butyleneglycols, and use propyl carbinol 2.60 especially, and all the other are all identical with embodiment 7, and making number-average molecular weight is 20,000, and gel content is the polyurethane particles of 0 (weight) %.Use this polyurethane particles, on pressure forming machine, make the plate that thickness is 100 μ m, make test film, measure photostabilization by this plate.It the results are shown in table 1.
Comparative example 5
679.6 parts of polytetramethylene carbonate diols that embodiment 1 is made and 4,4 ,-diphenylmethanediisocyanate (MDI) is packed into for 110.5 parts and is had in the reactor of whipping appts, thermometer and cooling tube, in 60 ℃ of reactions 2 hours, obtains the prepolymer of NCO end.With two liquid mixing machines (TT-1001, Japan, ォ-ト マ シ-Application exploitation society system), will heat prolongs 1 of agent to 80 ℃ pre-polymer solution with as normal temperature, 8.15 parts of 4-butyleneglycols and as 1.5 parts of mixing of propyl carbinol of normal temperature end-capping reagent.Then, with in establish kneader the laboratory with omnipotent extrusion machine (LABO with omnipotent extrusion machine KR-35 type, Japan, the loose chemical institute of large bamboo hat with a conical crown and broad brim society system), 120 ℃ push sub-thread material bar with complete screw after, on tablets press, make pill.The number-average molecular weight of the urethane that makes is 80,000, and gel content is 0 (weight) %.Use this polyurethane particles, make the plate that thickness is 100 μ m on pressure forming machine, make test film by this plate, test piece has been dissolved when measuring photostabilization, can not measure its rerum natura, and it the results are shown in table 1.
Comparative example 6
Except using polymerized thylene carbonate hexyl diol ester (ォ Le ボ ジ ォ-Le D-2000, synthetic society of Japan, East Asia system) outside the polytetramethylene carbonate diol that replaces making, other is all identical with comparative example 5, and making number-average molecular weight is 80,000, gel content is the polyurethane particles of 0 (weight) %.Use this polyurethane particles, on pressure forming machine, make the plate that thickness is 100 μ m, make test film, measure photostabilization by this plate.It the results are shown in table 1.
Table 1
| Urethane is formed | The number-average molecular weight of urethane | Photostabilization | ||
| Xanthochromia matter (△ e value) | Film toughness conservation rate (%) | |||
| Embodiment 7 | ?HDI/C4-PCDL/ ????1，4-BD | ????85000 | ????1.7 | ????75 |
| Embodiment 8 | Hydrogenation MDI/C4-PCDL/1,4-BD | ????80000 | ????1.7 | ????75 |
| Embodiment 9 | ?HDI/C4-PCDL/ ????1，4-BD | ????40000 | ????1.8 | ????74 |
| Comparative example 4 | ????HDI/C4 ????PCDL/ ????1，4-RD | ????20000 | Because of dissolving can not be measured rerum natura | |
| Comparative example 5 | ?MDI/C4-PCDL/ ????1，4-BD | ????80000 | ????20.5 | ????40 |
| Comparative example 6 | ?MDI/C6-PCDL/ ????1，4-BD | ????80000 | ????23.5 | ????45 |
Annotate: HDI: hexamethylene diisocyanate
Hydrogenation MDI: dicyclohexyl methyl hydride-4,4 '-vulcabond
MDI:4,4 ' diphenylmethanediisocyanate
C
4-PCDL: polytetramethylene carbonate diol
C
6-PCDL: poly-carbonic acid hexylene glycol ester
1,4-BD:1,4-butyleneglycol
Embodiment 10
2050 parts of the polytetramethylene carbonate diols that embodiment 1 is made, dimethyl formamide pack into for 6396 parts have reflux cooler, temperature is taken into account in the reactor of whipping appts, after fully mixing, add 4,4,524 parts of-methylene-biss (cyclohexyl diisocyanate) (hydrogenation MDI), dibutyltin dilaurate 20ppm, in 80 ℃ of reactions 3 hours, obtain the prepolymer of NCO end.Add isophorone diamine (IPDA) 163.06 parts, carry out about 2 hours after the chain extension reaction, add, continue reaction 1 hour as 8.85 parts of the dibutylamine of reaction terminating agent.Solid state component accounts for 30% in the polyurethane solution that obtains, and its number-average molecular weight is 80,000, and gel content is 0 (weight) %.
Then, the polyurethane solution that makes is coated on the sheet glass, in 80 ℃ through after 15 hours dryings, further in following 50 ℃ of dryings of decompression 4 hours, obtain the diaphragm that thickness is 100 μ m again.Mensuration makes that diaphragm-operated is anti-to add water decomposition, oil resistant acidity, and alcohol resistance, the results are shown in table 2.
Embodiment 11
Except replacing the hydrogenation MDI with different Buddhist ketone vulcabond, other is all identical with embodiment 10, makes that solids fraction accounts for 30%, number-average molecular weight is 80,000, gel content is the poly-propylhomoserin solution of 0 (weight) %.This polyurethane solution is coated on the sheet glass, obtains the diaphragm that thickness is 100 μ m similarly to Example 10.Mensuration makes anti-water decomposition, oil resistant acidity and the alcohol resistance of adding of diaphragm-operated.It the results are shown in table 2.
Comparative example 7
Except using polymerized thylene carbonate hexyl glycol (D-2000, Japan, the synthetic society in East Asia system) replace outside the polytetramethylene carbonate diol, other is all identical with embodiment 10, makes polyurethane solution, this polyurethane solution is coated on the sheet glass, obtains the diaphragm that thickness is 100 μ m similarly to Example 10.Measure anti-water decomposition, oil resistant acidity and the alcohol resistance of adding of gained diaphragm-operated.It the results are shown in table 2.
Comparative example 8
Except using poly-hexylene glycol lactone (ペ ラ Network セ Le 22N, Japan, ダ ィ セ Le chemistry society system) to replace outside the polytetramethylene carbonate diol, other is all identical with embodiment 10, makes polyurethane solution.Identical with embodiment 10, this polyurethane solution is coated in makes the diaphragm that thickness is 100 μ m on the sheet glass.Measure anti-water decomposition, oil resistant acidity and the alcohol resistance of adding of gained diaphragm-operated.The results are shown in table 2.
Comparative example 9
Except using polytetramethylene glycol (PTMG-2000, Japan, Mitsubishi change into society's system) to replace outside the polytetramethylene carbonate diol, other is all identical with embodiment 10, makes polyurethane solution.Identical with embodiment 10, this polyurethane solution is coated on the sheet glass, make the diaphragm that thickness is 100 μ m.Measure anti-water decomposition, oil resistant acidity and the alcohol resistance of adding of gained diaphragm-operated.The results are shown in table 2.
Comparative example 10
The consumption that removes isophorone diamine becomes 168.1 parts, and the consumption of dibutylamine becomes 2.83 especially, and other are all identical with embodiment 10, make that a kind of solids fraction accounts for 30%, number-average molecular weight is 250,000 polyurethane solution, its viscosity increased when synthetic, so that can not stir.
Comparative example 11
Except replace the IPDA as the chain extension agent with trihydroxymethyl propane, other are all identical with embodiment 10, and the synthetic of polyurethane solution tested.Consequently, begin to prolong reaction in case add the chain extension agent, find promptly that soon viscosity sharply rises, polymkeric substance sticks on the stirring rod of whipping appts, so that can not stir.
Table 2
Annotate: hydrogenation MDI: dicyclohexyl methyl hydride-4,4 ' vulcabond
| Urethane is formed | The average molecular weight of urethane number | ||
| Embodiment 10 | Hydrogenation MDI/C 4-PCDL/ ????IPDA | ????80000 | |
| Embodiment 11 | ??IPDI/C 4-PCDL/ ????IPDA | ????80000 | |
| Comparative example 7 | Hydrogenation MDI/C 6--PCDL/ ????IPDA | ????80000 | |
| Comparative example 8 | Hydrogenation MDI/PCL/ IPDA | ????80000 | |
| Comparative example 9 | Hydrogenation MDI/PTMG/ IPDA | ????80000 | |
| Comparative example 10 | Hydrogenation MDI/C 4-PCDL/ ????IPDA | ????250000 | |
| Comparative example 11 | Hydrogenation MDI/C 4-PCDL/ ????TMP | ??????- |
C
4-PCDL: polytetramethylene carbonate diol
IPDA: different Fo Er copper diamines
IPDI: different Fo Er copper vulcabond
C
6-PCDL: poly-carbonic acid hexylene glycol ester
PCL: poly-hexylene glycol lactone
PTMG: polytetramethylene glycol
TMP: TriMethylolPropane(TMP)
Table 2 (continuing)
| The anti-water decomposition molecular weight conservation rate (%) that adds | Oil resistant acidity | Alcohol resistance | ||
| Swelling capacity (%) | Strength retention (%) | Swelling capacity (%) | Strength retention (%) | |
| ????99 | ????10 | ????85 | ????10 | ????90 |
| ????99 | ????10 | ????87 | ????10 | ????90 |
| ????98 | ????42 | ????23 | ????20 | ????23 |
| ????7 | ????50 | ????15 | Dissolving | ????0 |
| ????55 | Dissolving | ????0 | Dissolving | ????0 |
| Synthetic medium viscosity rises, and can not stir, so that can't measure rerum natura | ||||
| Synthetic medium viscosity rises, and can not stir consequently and can't measure rerum natura | ||||
Embodiment 12
Apply the polyurethane solution that is made by embodiment 10 on silicon paper surface, making its dry thickness is 45 μ m, and heat drying forms the polyurethane skin rete then.Applying overlay capacity on this poly-ammonia skin membrane is 130g/m
2, thickness is that the tackiness agent of 118 μ m forms the polyurethane adhesive layer.This tackiness agent is at isophorone diisocyanate (IPDI)/polytetramethylene glycol (PT-MG-2000, Japan, Mitsubishi change into society's system)/N-(2-hydroxyethyl) propylene diamine/monoethanolamine/hydrazine hydrate (mol ratio: 20/10/5/4/2) in the host of Zu Chenging, added the PTMG class two liquid type polyurethane tackiness agent of hydrogenation Xylene Diisocyanate as linking agent.On this adhesive linkage, fit as the rise hair side of synthetic leather with the cotton nylon loop of base material, in 120 ℃ of heating 4 minutes, adhesive reaction is solidified after, silicon paper release paper is peeled off, make the lamination synthetic leather.Fig. 2 illustrates the longitudinal diagram of the lamination synthetic leather of gained.Among Fig. 2,1 presentation layer is pressed into the leather base material, 2 expression polyurethane adhesive layers, 3 expression thermoplastic polyurethane skin membranes.The rerum natura of this synthetic leather that evaluation makes.The results are shown in table 3.
Embodiment 13
Except the urethane solvent that the polyurethane solution replacement embodiment 10 that makes with embodiment 11 makes, other is all identical with embodiment 12, makes the lamination synthetic leather, estimates the rerum natura of this synthetic leather.The results are shown in the table 3.
Comparative example 12
Except the polyurethane solution that the polyurethane solution replacement embodiment 10 that makes with comparative example 7 makes, other is all identical with embodiment 12, makes the lamination synthetic leather, estimates the rerum natura of this synthetic leather.The results are shown in table 3.
Comparative example 13
Except the polyurethane solution that the polyurethane solution replacement embodiment 10 that makes with comparative example 8 makes, other is all identical with embodiment 12, makes the lamination synthetic leather, estimates this synthetic leather rerum natura.The results are shown in table 3.
Comparative example 14
Except the polyurethane solution that the polyurethane solution replacement embodiment 10 that makes with comparative example 9 makes, other is all identical with embodiment 12, makes the lamination synthetic leather, estimates this synthetic leather rerum natura.The results are shown in table 3.
Table 3
Annotate: hydrogenation MDI: dicyclohexyl methyl hydride-4,4 ' vulcabond
| Urethane is formed | Anti-ly add water decomposition | Oil resistant acidity | Alcohol resistance | |
| Embodiment 12 | Hydrogenation MDI/C 4- PCDL/IPDA | No abnormal | No abnormal | No abnormal |
| Embodiment 13 | ??IPDI/C 4- PCDL/IPDA | No abnormal | No abnormal | No abnormal |
| Comparative example 12 | Hydrogenation MDI/C 6- PCDL/IPDA | No abnormal | The surface dry spot is many | The dry spot on surface is many |
| Comparative example 13 | Hydrogenation MDI/ PCL/IPDA | Sur-face peeling | Sur-face peeling | Sur-face peeling |
| Comparative example 14 | Hydrogenation MDI/ PTMG/ IPDA | The dry spot on surface is many | Sur-face peeling | Sur-face peeling |
C
4-PCDL: polytetramethylene carbonate diol
IPDA: different Fo Er copper diamines
IPDI: different Fo Er copper vulcabond
C
6-PCDL: poly-carbonic acid hexylene glycol ester
PCL: poly-hexylene glycol lactone
PTMG: polytetramethylene glycol
Embodiment 14
The polyethylene terephthalate of 0.1 denier monofilaments that makes by the direct spinning method is (hereinafter to be referred as " PET ".) fiber is cut into 3mm length, prepare simultaneously polyvinyl alcohol (hereinafter to be referred as " PVA ") 1 dawn fineness, be cut into the staple fibre of long 3mm, PET fiber/PVA fiber by weight: 70/30 mixes, and starches legal system to get 2 weight per unit areas be 80g/m with copying
2Sheet.
Between these two sheets, inserting the plain weave organization unit area weight of being made up of the PET fiber false twist yarn of the long monofilament in 75 dawn/36 with sandwich-like is 50g/m
2Fabric, the form layers lamination.From the surface and the inside of this lamination sheets, alternatively the pressure that comes out with the many nozzles with 0.2mm hole is 15kg/cm
2Injection water handle, make superfine fiber and fabric fully ternary hand over to mix, make and mix sheet.
Then, this is mixed the sheet drying after, with the resinder that 240 order sand paper are housed fluffed separately in this surface that mixes sheet and the inside.(concentration: 20-30 weight %), its thickness is 0.1mm, and dry to play the aqueous solution that applies Walocel MT 20.000PV (CMC) on the hair side with scraper in this inside side that mixes sheet then.
On the other hand, the polyurethane solution that embodiment 10 is made dilutes with dimethyl formamide, the urethane solids fraction is adjusted to 15 (weight) %, solids fraction with respect to above-mentioned urethane, (SF 8427 to add 10 (weight) % surfactant, Japan, eastern レ ダ ゥ ユ-ニ Application ゲ シ リ ユ Application society system), make the coating composition of urethane.
In the solution of this polyurethane coating composition, immersion coating have above-mentioned CMC mix sheet after, in 20 ℃ water, solidify, dry then.Thereafter, be placed on boiling water 20 minutes, after removing PVA fiber and CMC, drying obtains flap.
With locomotive formula dyeing machinery, with dispersed dye (trade(brand)name: ス ミ カ ロ Application レ ッ ト (Sumikaron Red)-SBL) Sumitomo Chemical society system) with this flap dyeing with respect to flap weight 10 (weight) %, then, use with respect to the bisulfite sodium reduction of flap weight 5 (weight) % and clean.And then, static inhibitor (trade(brand)name: Na ィ ス Port Le (Nicepole) FE-18 at esters of acrylic acid, Japan, solar corona chemistry society system) and the hydrophobizing agent (trade(brand)name: ァ サ ヒ ガ-ト (Asahiguard) AG-770 of silicon class, Japan, the rising sun add ラ ス society system) 1 (weight) % aqueous dispersions in this flap of dipping, extrude immersion liquid with rolling machine strand after, with the pin tentering moisture eliminator that is set in 140 ℃ of temperature, the over feed rate(OFR) with 3%, 5 minutes residence time drying.The weight ratio of above-mentioned static inhibitor and water-resisting agent is 1: 1.
The flap that makes has the compact surfaces piloerection of imitative chamois leather style, keeps good gloss, and being clamminess property does not demonstrate good feel.Estimate anti-water decomposition, the oil resistant acidity and the alcohol resistance of adding of this flap.The results are shown in the table 4.
Embodiment 15
Except the polyurethane solution that the polyurethane solution replacement embodiment 10 that makes with embodiment 11 makes, other is all identical with embodiment 14, makes flap.Estimate anti-water decomposition, the oil resistant acidity and the alcohol resistance of adding of this flap.The results are shown in the table 4.
Comparative example 15
Except the polyurethane solution that the polyurethane solution replacement example 10 that makes with comparative example 7 makes, other is all identical with embodiment 14, makes flap.Estimate anti-water decomposition, oil resistant acidity and the alcohol resistance of adding of this flap.The results are shown in the table 4.
Comparative example 16
Except the polyurethane solution that the polyurethane solution replacement embodiment 10 that makes with comparative example 8 makes, other is all identical with embodiment 14, makes flap.Estimate anti-water decomposition, oil resistant acidity and the alcohol resistance of adding of this flap.The results are shown in the table 4.
Comparative example 17
Except the polyurethane solution that the polyurethane solution replacement embodiment 10 that makes with comparative example 9 makes, other is all identical with embodiment 14, makes flap.Estimate anti-water decomposition, oil resistant acidity and the alcohol resistance of adding of this flap.The results are shown in the table 4.
Table 4
| Urethane is formed | Anti-ly add water decomposition | Oil resistant acidity | Alcohol resistance | |
| Embodiment 14 | Hydrogenation MDI/C 4- ??PCDL/IPDA | Be not clamminess | Be not clamminess | Be not clamminess |
| Embodiment 15 | ????IPDI/C 4- ??PCDL/IPDA | Be not clamminess | Be not clamminess | Be not clamminess |
| Comparative example 15 | Add water MDI/C 6- ??PCDL/IPDA | Viscosity is big | Viscosity is big | Viscosity is big |
| Comparative example 16 | Hydrogenation MDI/ PCL/IPDA | Viscosity is big | Viscosity is big | Viscosity is big |
| Comparative example 17 | Hydrogenation MDI/ PTMG/IPDA | Be clamminess slightly | Viscosity is big | Viscosity is big |
Annotate: hydrogenation MDI: dicyclohexyl methyl hydride-4,4 ' vulcabond
C
4-PCDL: polytetramethylene carbonate diol
IPDA: different Fo Er copper diamines
IPDI: different Fo Er copper vulcabond
C
6-PCDL: poly-carbonic acid hexylene glycol ester
PCL: poly-hexylene glycol lactone
PTMG: polytetramethylene glycol
Description of drawings
Fig. 1 is the IR spectrogram of the polytetramethylene carbonate diol that makes by embodiment 1 method.
Fig. 2 is dissolved in the organic solvent with the urethane that polytetramethylene carbonate diol, fatty acid ester and chain extension agent that the inventive method makes obtain, and the coating composition that forms is coated in synthetic scytoblastema with on the leather material, and dry back forms epidermal area and the longitudinal diagram of the lamination synthetic leather (product that embodiment 12 makes) that makes.In Fig. 2, the 1st, lamination synthetic leather base material, the 2nd, polyurethane adhesive layer, the 3rd, thermoplastic polyurethane skin membrane.
As the inventive method, promptly adopt the new manufacturing method of the polytetramethylene carbonate diol of acidic cpd, suppressed side reaction significantly, can obtain purpose product dibasic alcohol by high yield.
Selectivity is used the polytetramethylene carbonate diol that makes by the inventive method, and only selected aliphatic diisocyanate for use and the prepolymer that makes as dibasic alcohol, prolong with the chain extension agent, therefore can make photostabilization, hydrolytic resistance, oil resistant acidity and all good thermoplastic polyurethane of alcohol resistance, this thermoplastic polyurethane can be advantageously used in coating composition, purposes such as lamination synthetic leather that obtains with this coating composition processing base material and dipping combined artificial leather.
Claims (6)
1. the manufacture method of the polytetramethylene carbonate diol of following formula (1) expression is characterized in that, in the presence of acidic cpd, makes 1, the 4-butyleneglycol with, from dialkyl carbonate, the carbonate reaction that chooses in diaryl carbonate and the alkylene carbonate;
(in the formula, P is the number with mean value of 3-85).
2. manufacture method according to claim 1 is characterized in that, acidic cpd is from phosphoric acid, phosphorous acid, phosphoric acid ester, and phosphorous acid ester, what choose in the acid phosphoric acid ester is at least a.
3. manufacture method according to claim 1 is characterized in that, the amount of acidic cpd, and with respect to 1, the total weight of 4-butyleneglycol and carbonic ether is 1ppm-10,000ppm.
4. manufacture method according to claim 1 is characterized in that the number-average molecular weight of polytetramethylene carbonate diol is 500-10,000.
5. number-average molecular weight is 500-10,000, and the method for making of the polytetramethylene carbonate diol of following formula (1) expression,
(in the formula, P is the number with mean value of 3-85)
It is characterized in that in the presence of acidic cpd, making number-average molecular weight is the polytetramethylene carbonate diol of 300-1000 and from dialkyl carbonate, diaryl carbonate, the carbonic ether that chooses in the alkylene carbonate reacts.
6. number-average molecular weight is 500-10,000, and the method for making of the polytetramethylene carbonate diol of following formula (1) expression,
(in the formula, P is the number with mean value of 3-85)
It is characterized in that making number-average molecular weight is that the polytetramethylene carbonate diol of 300-1000 carries out own condensation reaction in the presence of acidic cpd.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96112432 CN1153791A (en) | 1996-10-15 | 1996-10-15 | Process for preparing polytetramethylene carbonate diol |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96112432 CN1153791A (en) | 1996-10-15 | 1996-10-15 | Process for preparing polytetramethylene carbonate diol |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN93118583A Division CN1102189A (en) | 1992-09-29 | 1993-10-23 | Thermoplastic polyurethane derived from polytetramethylene carbonate diol |
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| Publication Number | Publication Date |
|---|---|
| CN1153791A true CN1153791A (en) | 1997-07-09 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 96112432 Pending CN1153791A (en) | 1996-10-15 | 1996-10-15 | Process for preparing polytetramethylene carbonate diol |
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| CN (1) | CN1153791A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102787448A (en) * | 2012-07-26 | 2012-11-21 | 东华大学 | Preparation method of degradable polycarbonate butanediol ester electrospinning fiber films |
| CN101855270B (en) * | 2007-11-16 | 2014-03-12 | 旭化成化学株式会社 | Polycarbonate diol |
| CN107722251A (en) * | 2012-12-26 | 2018-02-23 | 三菱化学株式会社 | Polyurethane obtained from PCDL and use PCDL |
-
1996
- 1996-10-15 CN CN 96112432 patent/CN1153791A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101855270B (en) * | 2007-11-16 | 2014-03-12 | 旭化成化学株式会社 | Polycarbonate diol |
| CN102787448A (en) * | 2012-07-26 | 2012-11-21 | 东华大学 | Preparation method of degradable polycarbonate butanediol ester electrospinning fiber films |
| CN102787448B (en) * | 2012-07-26 | 2015-06-03 | 东华大学 | Preparation method of degradable polycarbonate butanediol ester electrospinning fiber films |
| CN107722251A (en) * | 2012-12-26 | 2018-02-23 | 三菱化学株式会社 | Polyurethane obtained from PCDL and use PCDL |
| US11220572B2 (en) | 2012-12-26 | 2022-01-11 | Mitsubishi Chemical Corporation | Polycarbonate diol and polyurethane using same |
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