CN107089921A

CN107089921A - Orthoformic acid organic amine salt compounds and its purposes as foaming agent

Info

Publication number: CN107089921A
Application number: CN201610387866.1A
Authority: CN
Inventors: 毕戈华; 毕玉遂; 陈唐建; 翟志强
Original assignee: ZIBO ZHENGHUA FOAM MATERIAL CO Ltd
Current assignee: Xintai BuTian New Material Technology Co. Ltd.
Priority date: 2016-06-02
Filing date: 2016-06-02
Publication date: 2017-08-25
Anticipated expiration: 2036-06-02
Also published as: CN107089921B

Abstract

Orthoformic acid organic amine salt compound with below general formula (I)：A^n‑[B^m+]_p(I) in formula, A^n‑It is primitive nail acid group；B^m+Be or comprising：Ammonium ion and/or organic amine B cations；Wherein m=1 10；

Description

Orthoformic acid organic amine salt compounds and its purposes as foaming agent

Technical field

The present invention relates to being used as CO₂The organic ammonium salt compounds and its use as foaming agent of the anion of donor On the way, more specifically there is provided not only have to be used as CO₂The anion of donor and with hydroxyalkyl or hydroxyalkyl alkoxy base The new organic ammonium of solubilizing group is used as solubilizing group or C2-C14 alkyl (such as 2- chloroethyls, 3- chloropropyls or phenethyl) Salt compounds, and its in the expanded material such as material such as polyurethane foam or PVC foam material or foamed polystyrene Using.

Technical background

Hard polyurethane foam is as a kind of macromolecule new material, and its light weight, intensity are high and with extremely low thermal conductivity, are excellent The heat-insulating material of matter, is widely used in cold-storage insulation, especially chemical weapons cold-storage insulation, building energy conservation, solar energy, vapour The industries such as the household electrical appliances such as car, refrigerator ice cabinet.Most important raw material is foaming agent in hard polyurethane foam production.These current foaming agents are removed All it is chlorofluorocarbon material beyond pentamethylene, because their destructions to atmospheric ozone layer are so national governments sign already The international convention of " Montreal Protocol book ", limits and is phased out, forbids the production of such product and use, China is also this The signatories to a treaty of memorandum of agreement.

China is also using second generation chlorofluorocarbon blowing agent H CFC-141b (a fluorine dichloroethanes) and ring penta at present Alkane, the developed country such as America and Europe prohibits the use of HCFC-141b already, and Chinese Government just freezes HCFC-141b consumption figure for 2013 Knot in the level of consumption of 2009 and 2010,2015 eliminate freeze 20% consumption figure, and promise be advanced to 2025 Total ban is produced and used, and the developed country such as current America and Europe uses third generation blowing agents pentafluoropropane (HFC-245fa) With 3-pentafluorobutane (HFC-365), the GWP (chamber effect potential value) of second and third generation foaming agent is very high, to atmospheric ozone layer Destruction is serious, therefore America and Europe will forbid the use of third generation blowing agents before 2017.For this Honeywell Inc. of U.S. again It has developed forth generation physical blowing agent chlorotrifluoropropylene (LBA), but the valuable product, the ODP (destructions to ozone layer Latent energy value) although being zero, GWP still higher, it is more relatively environment-friendly than the third generation.These physics in addition to pentamethylene in a word Foaming agent is all the arch-criminal for destroying atmospheric ozone layer, because all chloride fluorine element, will all be eliminated.

Prior art discloses directly by CO₂As polyurethane foams, still, in view of CO₂The escape of gas is with it in original Expect that the solubility in MDI and PEPA and/or PPG is bad so that CO₂Gas can not in composition, foam It is uniformly dispersed, and foaming process is not easily controlled.

In addition, prior art discloses directly using a small amount of water as polyurethane foams, still, in view of the hydrogen of hydrone Key is acted on and solubility of the water in PEPA and/or PPG is bad, and hydrone is present in the form of droplet In composition, foam (such as polyether polyatomic alcohol component), local excessive is caused to react and foam in expanded material.If made with water For foaming agent, then more urea bond is included in polyurethane foamed material, the intensity and heat-insulating property of foamed material is largely effected on. If in addition, being improved slightly as the consumption of the water of foaming agent, the performance and size of polyurethane foam can be significantly impacted Stability.If using water as unique foaming agent, polyurethane foam, which is known from experience, meets with asking for contraction, incipient scorch and poor insulation property Inscribe (shrinkage, scorching, inadequate heat insulation).

In a word, foaming agent of the prior art can not be dispersed in composition, foam with molecular level, so as to cause bubble The size of the uniform abscess of skewness in hole is uneven, eventually affects the strength character and thermal insulating properties of expanded material.

The content of the invention

To overcome shortcoming present in prior art, goal of the invention of the invention be to provide a kind of polyurethane foams and its Preparation method, chlorofluorocarbon, will not destroy atmospheric ozone layer.

It is an object of the invention to provide not only have to be used as CO₂The anion of donor and with hydroxyalkyl or hydroxyalkyl alkane Epoxide group is used as solubilizing group or C₂-C₁₄Alkyl (such as 2- chloroethyls, 3- chloropropyls or phenethyl) is used as the new of solubilizing group Type organic ammonium salt compounds, and its in expanded material such as polyurethane foam or PVC foam material or polystyrene foam Application in material.

The new organic ammonium salt compounds are suitable as foaming agent.It produces CO in foaming process₂Gas.The application Inventor it was unexpectedly observed that being used as CO₂The anion with-n valencys of donor easily decomposes produce CO at elevated temperatures₂ Gas, or even when being foamed at a lower temperature, it is described below to be used as CO₂The anion with-n valencys of donor can By NCO group activation of the isocyanate-monomer as contained by MDI and TDI, quick release goes out CO₂Gas.Further, since with solubilising Group so that foaming agent can be substantially soluble in foaming raw material (such as PPG or PEPA) or with foaming raw material it Between have good intersolubility, foaming agent of the invention can be homogeneously dispersed in equably to foam in composition, foam, The distribution of abscess is also than more uniform in polyurethane foam, and abscess size than more uniform.In addition, the foaming agent of the present invention Compound contains hydroxyl and/or amino, is decomposed in the foaming agent and discharges CO₂Catabolite produced afterwards still contains hydroxyl Base and/or amino, when the molecular weight of catabolite is relatively low, they are suitable as chain extender or crosslinking agent occurs with isocyanates Reaction forms polymer, and when the molecular weight of catabolite higher (such as number-average molecular weight is 100-3000), they can be replaced For a part of PEPA or PPG in composition, foam, for example prior art composition, foam basis The upper appropriate consumption for reducing PEPA or PPG.Those skilled in the art can be according to hair of the present invention The average hydroxyl value and PEPA of infusion or the average hydroxyl value of PPG come calculate foaming agent of the present invention consumption and The consumption of PEPA and/or PPG.Especially, in the process foamed using polyalcohol and polyisocyanates In, if using the organic ammonium salt compounds of the present invention as foaming agent, organic ammonium salt compounds are both as " foaming Point " is used as " chain extension point " and/or " crosslinking points " again, significantly enhances the mechanical strength and mechanical strength of abscess, and what is obtained is poly- Urethane foams have good dimensional stability.Therefore, based in terms of above three, the present invention is completed.

In this application, " it is used as CO₂The anion of donor " refers in case of heating or can in foaming process Decompose and discharge CO₂Anion.

There is provided the organic amine salt compound or organic with below general formula (I) according to the first embodiment of the present invention Amine salt compound mixture：

A^n- [B^m+]_p (I)

In formula, A^n-It is as CO₂The anion with-n valencys of donor, wherein n=1,2 or 3；

B^m+Be or comprising：+ 1 valency ammonium ion (⁺NH₄) and/or individual with m-⁺NR³R⁴H groups and/or-⁺NR³H- groups (that is, with m with⁺H combines to form the primary amine, secondary amine and/or tertiary amine group of cation) one or more organic amine B Cation (cation formed by one or more organic amine B), abbreviation organic amine cation；Wherein m=1-10, such as 1, 2nd, 3,4,5,6,7,8,9 or 10；

Wherein A^n-It is the one or more in following anion：

(a) carbamic acid root：R¹R²N-COO^-；

(b) carbonate：CO₃ ^2-；

(c) formate：HCOO^-；

(d) bicarbonate radical：HO-COO^-；

(e) organic (base) single carbon acid group：R^aO-COO^-, wherein R^aIt is the C optionally replaced by hydroxyl or amino or halogen₁-C₂₆ Alkyl (preferably C₁-C₁₀Alkyl, more preferably C₁-C₃Alkyl), C₁-C₂₆Acyl group (preferably C₁-C₁₀Acyl group, more preferably C₁-C₂Acyl group)；

(f) organic (base) polyamino formate：^-OOC-N(R¹)-R^b-N(R²)-COO^-, or R^b'(-N(R¹)-COO^-)₃,

In formula, R^bIt is the C optionally replaced by hydroxyl or amino or halogen₁-C₁₆Alkylene (preferably C₂-C₁₀It is alkylene, more excellent Select C₂-C₆Alkylene, such as-CH₂-CH₂-), R^b' it is the trivalent C optionally replaced by hydroxyl or amino or halogen₂-C₂₀Alkyl is (more excellent Select trivalent C₃-C₁₅Alkylene, such as-CH₂-CH(CH₂-)-CH₂- etc.)；

(g)(i.e. HC (OR ') O₂ ^2-), or(i.e. HCO₃ ^3-),

In formula, R ' is H, the C optionally replaced by hydroxyl or amino or halogen₁-C₂₆Alkyl (preferably C₁-C₁₀Alkyl, more preferably C₁-C₃Alkyl), C₁-C₂₆Acyl group (preferably C₁-C₁₀Acyl group, more preferably C₁-C₇Acyl group)；Or

(h) organic (base) many carbonates：^-OOC-ORcO-COO^-,

In formula, R^cIt is the C optionally replaced by hydroxyl or amino or halogen₁-C₂₆Alkylene (preferably C₂-C₁₀It is alkylene, more excellent Select C₂-C₆Alkylene)；

Wherein, R¹,R²,R³Or R⁴Independently selected from：H, R, the C optionally replaced by hydroxyl or amino or halogen₁-C₇Aliphatic Alkyl (preferably C₁-C₄Alkyl), the C optionally replaced by hydroxyl or amino or halogen₃-C₇Cyclic aliphatic alkyl (such as cyclobutyl or hexamethylene Base), or, the C optionally replaced by hydroxyl or amino or halogen₆-C₁₀Aromatic hydrocarbyl (preferably phenyl or aminomethyl phenyl)；

Precondition is：The R in the compound of above-mentioned logical formula (I)¹,R²,R³Or R⁴In at least one be to be connected with N atoms R group (i.e. N-R groups), or the logical formula (I) compound have at least one R group bonded with N (i.e. at least one N-R groups)；

Wherein one or more of the R group in following groups：

(1a)H[OCH(R_1a)CH(R_2a)]_q-, such as H (OCH₂CH₂)_q-、H(OCH₂CH(CH₃))_q-、H(OCH(CH₃)CH₂ )_q-、H(OCH₂CH(C₆H₅))_q-、H(OCH(C₆H₅)CH₂)_q-、H(OCH₂CH(CH₂Cl))_q-、H(OCH(CH₂Cl)CH₂)_q- or H (OCH₂CH(CBr₃))_q-；

(2a)H[OCH(R_1a)CH(R_2a)CH(R_3a)]_q-；Or

(3a)H[OCH(R_1a)CH(R_2a)CH(R_3a)CH(R_4a)]q-；

Wherein q value or average value are q=1-50, preferably 1-20, more preferably 1-5, more preferably q=1-4, more preferably q= 1-3, particularly preferred q=1-2.5, particularly preferred q=1.5-2.0, by q mean value calculation, or q is 5-50, more preferably 10- 20；R_1a、R_2a、R_3aOr R_4aIt is each independently selected from：H, the C optionally replaced by hydroxyl or amino or halogen₁-C₇Aliphatic alkyl, The C optionally replaced by hydroxyl or amino or halogen₃-C₇Cyclic aliphatic alkyl (such as cyclobutyl or cyclohexyl), or, optionally by hydroxyl or Amino or the C of halogen substitution₆-C₁₀Aromatic hydrocarbyl (such as phenyl or aminomethyl phenyl).

That is, leading to formula (I) compound has at least one above-mentioned R group.

R group is identical or different with following groups：The C optionally replaced by hydroxyl or amino or halogen₁-C₇Aliphatic alkyl (preferably C₁-C₄Alkyl), the C optionally replaced by hydroxyl or amino or halogen₃-C₇Cyclic aliphatic alkyl (such as cyclobutyl or cyclohexyl), Or, the C optionally replaced by hydroxyl or amino or halogen₆-C₁₀Aromatic hydrocarbyl (preferably phenyl or aminomethyl phenyl).

In this application ,-⁺NR³R⁴H groups refer to-NR³R⁴⁺H groups ,-⁺NR³H- groups refer to-NR³(⁺H)-group.One As, organic amine B has >=m (such as m to m+3) primary amine, secondary amine and/or tertiary amine group, and optionally there is quaternary ammonium group Group.For example, CH₃CH₂ ⁺NH₂H (i.e. ethamine cation, CH₃CH₂NH₂ ⁺H it is) by ethamine and one⁺H ions are combined institute's shape Into, B here¹⁺=CH₃CH₂ ⁺NH₂H or CH₃CH₂NH₂ ⁺H, m=1, B=ethamine.In above formula, primary amine, secondary amine and/or tertiary amine Group is selected from-NR³R⁴Group and-NR³- group.

Organic amine compound B is primary amine, secondary amine and/or tertiary amine group with m to m+3, and optionally has season The organic amine of ammonium group.It is preferred that, organic amine compound B has 2-200 carbon atom (preferably 3-50, more preferably 3-20 Individual, more preferably 3-12) organic amine compound.Typically, it has above-described R group.

In this application, organic amine compound B, or the primary amine with >=m (such as m to m+3), secondary amine and/or Tertiary amine group and the organic amine compound B optionally with quaternary ammonium group, with m⁺H ions are combined and become B^m+。

Preferably, A^n-It is combination or the mixture for the two or more above-mentioned anion being selected from (a)-(h), and/ Or B^m+It is combination or the mixture of two or more above-mentioned organic amine cations, therefore, it is a kind of mixing to lead to formula (I) compound Thing.

In the application, p B^m+It may be the same or different, or p B may be the same or different.Preferably, p B^m+Difference, or p Individual B is different.

Therefore the present invention also provides a kind of foaming agent, and it includes organic amine salt compound or organic amine with logical formula (I) Salt compound mixture is made up of organic amine salt compound or organic amine salt compound mixture with logical formula (I).

Additionally, it is provided a kind of embodiment, wherein A^n-It is the one or more in following anion：(a)、(c)、 (d)、(e)、(f)；Or (h).

Typically, in logical formula (I), the single A with+2 or+trivalent^n-Can respectively with one or more B^m+Into salt.And, With multiple-N⁺R³R⁴H groups and/or-N⁺R³The single organic amine ion B of H- groups^m+Can be with one or more A^n-Into Salt.

For (c) HCOO^-For, ammonium formate or formic acid organic amine salt are more stable compound, decomposition temperature in itself Generally greater than 100 DEG C, the fusing point of such as ammonium formate is up to 116 DEG C.Ammonium formate or formic acid organic amine salt are used as poly- ammonia however, working as During ester foaming agent, it is found that they but become unstable when touching isocyanates (such as MDI), reason is that ammonium formate or formic acid have Machine amine salt generates labile acid anhydride group with NCO group reaction, carbon dioxide is then decomposed to give off rapidly, while also releasing Carbon monoxide.

Similarly, following anion also becomes unstable when touching isocyanates (such as MDI)：(e)R^aO-COO^-；(f)^- OOC-N(R¹)-R^b-N(R²)-COO^-Or R^b'(-N(R¹)-COO^-)₃；Or (h)^-OOC-OR^cO-COO^-；

It is preferred that, (e) R^aO-COO^-It is the moon formed by bicarbonate hydrocarbyl carbonate (such as bicarbonate methyl esters or bicarbonate ethyl ester) Ion or acid group.

It is preferred that, (f)^-OOC-N(R¹)-R^b-N(R²)-COO^-Or R^b'(-N(R¹)-COO^-)₃It is by (the amino of alkylene two respectively Formic acid) or alkylene three (carbamic acid) anion or acid group that are formed.

It is preferred that, (h)^-OOC-OR^cO-COO^-, it is by the carbonic acid of alkylene two (such as ethylene ammonium carbonate NH₄OOC- OCH₂CH₂O-COONH₄) anion or acid group that are formed.

It is preferred that, for example, when logical formula (I) compound is used to prepare the polyurethane foamed material of heat insulation-type as foaming agent, Especially the polyurethane foamed material of obturator-type when, from bubbling efficiency, the smell of foaming agent, heat-insulating property and abscess-size stability And the dimensional stability of polyurethane foam finished product considers that q=1-5, more preferably q=1-4, more preferably q=1-3 are especially excellent Q=1-2.5 is selected, particularly preferred q=1.5-2.0, by q mean value calculation.It is preferable, therefore, that B is two or moreization The mixture of compound.It is further preferred that including at least one N-H group (N-H covalent bonds, i.e. the H being connected with N) in B.

R¹,R²,R³And R⁴Independently selected from：H, R, the C optionally replaced by hydroxyl or amino or halogen₁-C₄Aliphatic alkyl (such as methyl or ethyl or propyl group), the cyclobutyl or cyclohexyl optionally replaced by hydroxyl or amino or halogen, or, optionally by hydroxyl Base or the phenyl or aminomethyl phenyl of the substitution of amino or halogen.

It is preferred that, R_1a、R_2a、R_3aOr R_4aIt is each independently selected from：H, the C optionally replaced by hydroxyl or amino or halogen₁-C₃ Aliphatic alkyl, the C optionally replaced by hydroxyl or amino or halogen₃-C₆Cyclic aliphatic alkyl, or, optionally by hydroxyl or amino or halogen The C of element substitution₆-C₇Aromatic hydrocarbyl (such as phenyl or aminomethyl phenyl).

It is further preferred that R_1a、R_2a、R_3aOr R_4aIt is each independently selected from：H, methyl or is optionally replaced by hydroxyl or amino or halogen Ethyl, or the propyl group or isopropyl optionally replaced by hydroxyl or amino or halogen optionally take by hydroxyl or amino or halogen The cyclohexyl in generation, or, the phenyl or aminomethyl phenyl optionally replaced by hydroxyl or amino or halogen.

It is further preferred that R_1a、R_2a、R_3aOr R_4aIt is each independently selected from：H, methyl, chloromethyl, bromomethyl, ethyl, cyclohexyl, Or, phenyl.

In general, the organic amine salt compound for leading to formula (I) contains alcohol amine compound or alcohol amine compound residue.Namely Say, the organic amine salt compound of logical formula (I) is that have as CO₂The anion A of donor^n-And contain alcohol amine compound or hydramine One or more organic amine salt compounds of compounds residues.

It is preferred that, A^n-It is the one or more in following anion：

(a)R¹R²N-COO^-；Wherein R¹And R²It is hydrogen, methyl, ethyl, methylol, ethoxy or hydroxypropyl independently of one another；

(b)CO₃ ^2-；

(c)HCOO^-；

(d)HO-COO^-；Or

(g)(i.e. HC (OR ') O₂ ^2-), or(i.e. HCO₃ ^3-),

In formula, R ' is H, the C optionally replaced by hydroxyl or amino or halogen₁-C₂₆Alkyl (preferably C₁-C₁₀Alkyl, more preferably Methyl, ethyl, propyl group), C₁-C₂₆Acyl group (preferably C₁-C₁₀Acyl group, more preferably formoxyl, acetyl group or propiono).

In this application, " optionally " represent to carry out or without representing substitution or not replacing." optional " indicate or No.

Typically, in the compound of logical formula (I), ammonia or amino and/or amido (i.e.-N in organic amine compound B⁺R³R⁴H Group and/or-N⁺R³H- groups) 50-100% by anion A^n-Neutralize, that is to say, that amino and/or amido into salt rate For 50-100%.It is preferred that, ammonia or amino and/or the 65-100% of amido in organic amine compound B are by anion A^n-Neutralize.More It is preferred that, ammonia or amino and/or the 75-100% of amido in organic amine compound B are by anion A^n-Neutralize.It is further preferred that ammonia or having The 75-90% of amino and/or amido in machine amines B is by anion A^n-Neutralize.

The pH of logical formula (I) compound is generally 7.5-10, it is preferable that be pH 7.8-9.5, more preferably pH 8-9.For example, working as Ammonia or amino and/or amido (i.e.-N in organic amine compound B⁺R³R⁴H groups and/or-N⁺R³H- groups) 50-95% it is cloudy Ion A^n-During neutralization, now formula (1) compound is metastable.

When the amino and/or the 100% of amido in ammonia or organic amine compound B is by anion A^n-During neutralization, then lead to formula (I) Become below general formula：

In this application, for simplicity, with m (wherein m=1-10, such as 1,2,3,4,5,6,7,8,9 or 10 It is individual)-N⁺R³R⁴H groups and/or-N⁺R³The organic amine ion of H- groups may be considered the organic amine ion of+m valencys.

It is preferred that, for m (such as m=2-10, such as 3,4,5)-N⁺R³R⁴H groups and/or-N⁺R³H- groups Organic amine ion (B^m+), wherein compound B be by with least one (preferably at least two) N-H covalent bond (i.e. with least One reactive hydrogen bonded with N) organic amine compound (M) formed as initiation material.That is, in B or B^m+In N-R Group is by being replaced at least one N atom of the organic amine compound (M) by said one or multiple R groups Formed by.That is, compound B is the organic amine compound with N-R groups (or N-H covalent bonds).It is preferred that, with N-R bases The organic amine compound B of group be by least one N atom of the organic amine compound (M) by said one or Formed by multiple R groups replace.

Preferably, R¹And R²In at least one be H, more preferably R¹It is H and R²It is H.

It is preferred that, organic amine compound (M), i.e. with least one N-H (that is, N-H covalent bonds or with least one The bonded H with N, is reactive hydrogen) organic amine compound (M), be selected from following organic amine compound in these：

C₁-C₂₄Alkyl amine (primary amine class), such as methylamine, ethamine, propylamine, butylamine, amylamine, hexyl amine, heptyl amine, Octyl amine, nonyl amine, decyl amine, lauryl amine, tetradecylamine, hexadecylamine, octadecylamine, eicosyl amine, Tetracosyl amine, the aniline of unsubstituted or substituted (such as halogen substitution), the benzyl amine of unsubstituted or substituted (such as halogen substitution), Cyclo-hexylamine, methylcyclohexyl amine, cyclohexyl methyl amine, N- methylcyclohexyls amine or N- methylbenzylamines, etc.；

Two (C₁-C₁₆Alkyl) amine (secondary amine class, the i.e. monoamine with a secondary amine), such as dimethylamine, diethyl Amine, Methylethyl amine, dipropylamine, methyl-propyl amine, ethyl propyl amine, dibutylamine, N-Ethylbutylamine, diamyl amine, two Hexyl amine, diheptyl amine, dioctylamine, dinonyl amine, didecylamine, two (dodecyl) amine, two (myristyl) amine, two (cetyl) amine, two (octadecyl) amine, two (eicosyl) amine or two (tetracosyl) amine, etc.；

Optionally in C₂-C₁₄The C being optionally substituted by a hydroxyl group on alkylene₂-C₁₄(two of which amido is each independent for alkylene Diamines Ground is primary amine groups or secondary amine), such as ethylenediamine, N- methyl ethylenediamines, N, N '-dimethyl ethylenediamine, 1,3- propane diamine, N- first Base, N ' ethyl -1,3- propane diamine, butanediamine (including various isomers, such as 1,2 or 1,3- or Putriscine), penta 2 ammoniums (bag Include various isomers), hexamethylene diamine (including various isomers), 3- methylols-hexamethylene diamine, heptamethylene diamine (including various isomers), 3- methylols-heptamethylene diamine, octamethylenediamine (including various isomers), 3,5- dihydroxy octamethylenediamines, nonamethylene diamine (including various isomeries Body), decamethylene diamine (including various isomers), 3,6- dihydroxy decamethylene diamines, dodecamethylene diamine, tetradecane diamines, p or m- benzene two Amine, 3,3 '-two chloro- 4,4 '-diphenylmethanediamiand (MOCA), or piperazine, etc.；

Optionally in C₂-C₁₄The C being optionally substituted by a hydroxyl group on alkylene₄-C₁₆Polyalkylenepolyamines class, such as diethylenetriamines, Trien, tetren, penten, dipropylenetriamine, tri propylidene tetramine, four propylidene five Amine, five inferior propyl hexamine, two butylidene triamines, three butylidene tetramines, the amine of four butylidene five, triethylenediamine, dimethyl two Ethyl triamine, three (2- hydroxyls -1,3- propylidene) tetramines or four (2- hydroxyls -1,3- propylidene) five amine；Deng；

The C being optionally optionally substituted by a hydroxyl group with three primary amine groups₃-C₁₈Organic three amine is optional with four primary amine groups The C being optionally substituted by a hydroxyl group₅-C₁₈Organic tetraamine, such as 1,3,5- triamidos-hexamethylene, 1,3,5- tri- (amino-ethyl)-hexamethylene Alkane, 1,3,5- tri- (aminopropyl) -1,3,5- hexahydrotriazines, 1,3,5- tri- (methyl amine propyl group) -1,3,5- hexahydrotriazines, Or, melamine, season penta tetramine, etc.；Or

C₂-C₁₀Alcamines, such as monoethanolamine, diethanol amine, monopropylene glycol amine, dipropanolamine, monoisopropanolamine, diisopropyl Hydramine, monobutanolamine, or two butanolamines, etc..

It is further preferred that (M) is selected from：

Methylamine, ethamine, propylamine, butylamine, amylamine, hexyl amine, the aniline of unsubstituted or substituted (such as halogen substitution), not Substitution or the benzyl amine of substitution (such as halogen substitution), cyclo-hexylamine, or methylcyclohexyl amine；

Dimethylamine, diethylamide, Methylethyl amine, dipropylamine, or methyl-propyl amine；

Ethylenediamine, N- methyl-ethylenediamine, N, N '-dimethyl ethylenediamine, 1,3- propane diamine, N- methyl, N ' ethyls -1,3- Propane diamine, butanediamine (including various isomers, such as 1,2 or 1,3- or Putriscine), penta 2 ammoniums (including various isomers), Hexamethylene diamine (including various isomers), 3- methylols-hexamethylene diamine, p or m- phenylenediamines, 3,3 '-two chloro- 4,4 '-diphenyl methane Diamines (MOCA), or piperazine；

Diethylenetriamines, trien, or tetren；

1,3,5- triamido-hexamethylene, 1,3,5- tri- (amino-ethyl)-hexamethylene, 1,3,5- tri- (aminopropyl) -1,3, 5- hexahydrotriazines, 1,3,5- tri- (methyl amine propyl group) -1,3,5- hexahydrotriazines, or, melamine, season penta tetramine；

Or

Monoethanolamine, monopropylene glycol amine, monoisopropanolamine, or monobutanolamine.

In general, B is worked as^m+Be except+1 valency ammonium ion (⁺NH₄) outside there are m (such as 2-10, such as 3,4,5 It is individual)-N⁺R³R⁴H groups and/or-N⁺R³(that is, B during the organic amine ion of H- groups^m+Be not +1 valency ammonium ion (⁺NH₄), i.e. When B is not ammonia), compound B is as initiation material or as initiator and epoxidation by above-mentioned organic amine compound (M) Thing (such as oxirane, expoxy propane, epoxychloropropane, epoxy bromopropane, epoxy butane or epoxy chlorobutane or styrene oxygen Compound, and any two or a variety of mixtures in them) reacted what is formed.

In addition, working as A^n-It is any one of (a), (b), (c), (d), (e), (f) or (h) and B^m+It is with m (such as 2-10, such as 3,4,5)-N⁺R³R⁴H groups and/or-N⁺R³(that is, B during the organic amine ion of H- groups^m+It is not +1 Valency ammonium ion (⁺NH₄), i.e. when B is not ammonia), the compound (I) is in solvent (preferably protonic solvent, alcohols solvent Or DMF) in, optionally in the presence of catalyst (such as ammoniacal liquor, or organic amine, such as ethamine, diethylamine or triethylamine), by selecting From one or more anion in (a), (b), (c), (d), (e), (f) or (h) and ammonium salt (such as amino first of ammonia formation Aminoquinoxaline (the R of sour ammonium, hydroxyalkyl or the substitution of hydroxyalkyl alkoxy¹R²N-COO^-+NH₄), ammonium carbonate (CO₃ ^2-(⁺NH₄)₂), carbon Sour hydrogen ammonium or ammonium formate, and two or more in them mixture) or with above-mentioned one or more organic amine compounds (M) Organic amine salt (the carbamic acid organic amine of such as carbamic acid organic amine salt, hydroxyalkyl or the substitution of hydroxyalkyl alkoxy of formation The mixture of salt, carbonic acid organic amine salt, bicarbonate organic amine salt, formic acid organic amine salt, and two or more in them), with Epoxides (such as oxirane, expoxy propane, epoxychloropropane, epoxy bromopropane, epoxy butane or styrene oxide, and Any two or a variety of mixtures in them) reacted what is formed.Typically, solvent described here be selected from it is following these In one or more, but be not limited to：Methanol, ethanol, ethylene glycol, ethylene glycol, molecular weight are less than 400 polyethylene glycol, molecule Polypropylene glycol, formamide, glycerine, formic acid glyceride or water of the amount less than 300.

In addition, working as A^n-It is (a) R¹R²N-COO^-Anion and B^m+Be+1 valency ammonium ion (⁺NH₄) when, the compound (I) it is R¹R²N-COO^-+NH₄, wherein R¹Or R²One or both of be above-mentioned R group.These compound Rs¹R²N-COO^-+NH₄ There is R group, therefore, logical formula (I) compound can be also directly used as or as foaming agent, certainly, these compound Rs¹R²N- COO^-+NH₄Also further it can be reacted with above-mentioned epoxides, obtain has alcohol amine compound or alcohol in cationic moiety The logical formula (I) compound of amine residue.

Typically, A is worked as^n-It is (g) anion and B^m+Be with m (such as 2-10, such as 3,4,5)-N⁺R³R⁴H groups And/or-N⁺R³(that is, B during the organic amine ion of H- groups^m+Be not +1 valency ammonium ion (⁺NH₄), i.e. when B is not ammonia), institute It is by orthoformic acid ester type compound in solvent (preferably protonic solvent, alcohols solvent or DMF), optionally to state compound (I) Ground is belonging to Organic Alcohol in the presence of catalyst (such as ammoniacal liquor, or organic amine, such as ethamine, diethylamine or triethylamine) Enter in the presence of the organic amine M of amine or the compound B and water that belong to Organic Alcohol amine with least one above-mentioned N-R group Row hydrolysis is formed.Preferably, the amount of the water is sufficient so that at least two of orthoformic acid ester type compound Ester group hydrolyses, it is further preferred that the amount of water is sufficient so that three ester group hydrolyses of orthoformic acid ester type compound.Primitive nail The hydrolyst of acid esters is usually alkali compounds, preferably organic amine.It is preferred that, with least one above-mentioned N-R group (i.e., At least one R group bonded with N) organic amine compound B be as the organic amine compound (M) described in ammonia or more with Upper described epoxides (for example oxirane, expoxy propane, epoxychloropropane, epoxy bromopropane, epoxy butane (including Various isomers such as 1,2- epoxy butanes, 2,3- epoxy butanes), epoxy chlorobutane (including various isomers such as 1,2- epoxies -4- Chlorobutane, 2,3- epoxies -1-chlorobutane) or styrene oxide, and any two or a variety of mixtures in them) carry out instead Should be prepared.In the R group, q average value (i.e. the degree of polymerization of epoxides) is as defined above.Q average value energy Enough selected according to the concrete application of polyurethane foamed material.It is preferred that, when the polyurethane foamed material for preparing heat insulation-type, Especially the polyurethane foamed material of obturator-type when, from bubbling efficiency, the smell of foaming agent, heat-insulating property and abscess-size stability And the dimensional stability of polyurethane foam finished product considers, q=1-5, more preferably q=1.2-4.5, more preferably q=1.3-4, Particularly preferred q=1.5-3.5, by q mean value calculation.

Preferably, orthoformic acid ester type compound is the one or more in these following compounds：(the C of primitive nail three₁- C₈) alkyl esters, the preferably (C of primitive nail three₁-C₇) alkyl esters, for example, trimethyl orthoformate, triethyl orthoformate, orthoformic acid first Base diethyl ester, tripropyl orthoformate, primitive nail acid methyl dipropyl, tributyl orthoformate, orthoformic acid triphen base ester, orthoformic acid Tribenzyl ester, acetyl group orthoformic acid diethyl ester, acetyl group orthoformic acid ethyl-methyl ester, orthoformic acid three (ethylene glycol) ester, primitive nail Sour three (diethylene glycol) esters, orthoformic acid three (triethylene glycol) ester, orthoformic acid three (tetraethylene glycol) ester, (polyethylene glycol of orthoformic acid three (degree of polymerization=5-10)) ester, orthoformic acid three (propane diols) ester, orthoformic acid three (DPG) ester, orthoformic acid three (tripropylene glycol) Ester, orthoformic acid three (four propane diols) ester, orthoformic acid three (polypropylene glycol (degree of polymerization=5-10)) ester.

It is preferred that, solvent used in the hydrolytic process of orthoformate is not selected from following one or more in these, but not It is limited to：Methanol, ethanol, ethylene glycol, ethylene glycol, molecular weight be less than 400 polyethylene glycol, molecular weight be less than 300 polypropylene glycol, Formamide, glycerine, formic acid glyceride or water.

In order to prepare the compound of above-mentioned logical formula (I), them can be prepared using a variety of preparation methods.As just act Example, describes several representational preparation methods separately below.

According to the second embodiment of the present invention, the present invention, which also provides to prepare to have, is used as CO₂The anion of donor The method of organic amine salt compounds, or prepare wherein A^n-It is any one of (a), (b), (c), (d), (e), (f) or (h) Or the method for the compound of the logical formula (I) described above of a variety of anion, this method includes the first raw material and the second raw material exists In solvent (preferably protonic solvent or alcohols solvent), optionally in catalyst (such as ammoniacal liquor, or organic amine, such as ethamine, two Ethamine or triethylamine) in the presence of, reacted, wherein the first raw material is one kind or many in these following compounds Kind：

R¹R²N-COONH₄, or R¹R²N-COOH organic amine compound (M) salt,

(NH₄)₂CO₃, or carbonic acid organic amine compound (M) salt,

HCOONH₄, or formic acid organic amine compound (M) salt,

HO-COONH₄(i.e. ammonium hydrogen carbonate), or organic amine compound (M) bicarbonate,

R^aO-COONH₄, or R^aO-COOH organic amine compound (M) salt,

NH₄OOC-N(R¹)-R^b-N(R²)-COONH₄, R^b'(-N(R¹)-COO)₃(NH₄)₃, HOOC-N (R¹)-R^b-N(R²)- COOH organic amine compound (M) salt, or R^b'(-N(R¹)-COOH)₃Organic amine compound (M) salt, or

NH₄OOC-OR^cO-COONH₄, HOOC-OR^cO-COOH organic amine compound (M) salt；

Second raw material is the one or more in these following compounds：

Or benzene Ethylene oxide (styrene oxide)；

Wherein R¹, R², R^a, R^b, R^b', R^cAs defined above, R_1a、R_2a、R_3aOr R_4aAs defined above, and organic amine Compound (M) is as defined above.

It is preferred that, preparing wherein A^n-Be (a)-(f) or (h) logical formula (I) the reaction of compound in, the first raw material and The mol ratio of two raw materials is usually 1:1.3-5, preferably 1:1.5-4.5, more preferably 1:1.6-4, such as 1:1.5 to 1:3.

It is preferred that, the first raw material is the one or more in these following compounds：

Aminoquinoxaline, carbamic acid organic amine M (abbreviation carbamic acid amine), amidocarbonic acid ammonium (R¹R²N-COO^-+NH₄), Amidocarbonic acid organic amine M salt (that is, R¹R²The salt of N-COOH and M formation, abbreviation amidocarbonic acid amine), ammonium carbonate, carbonic acid organic amine M Salt (that is, H₂CO₃With the salt of M formation, abbreviation amine carbonate), ammonium formate, formic acid organic amine M salt (that is, formic acid and the salt of M formation, letter Claim ammonium formate), ammonium hydrogen carbonate, bicarbonate organic amine M salt (that is, M bicarbonate, abbreviation Ammonium bicarbonate food grade), R^aO-COONH₄, R^aO-COOH M salt, NH₄OOC-N(R¹)-R^b-N(R²)-COONH₄, R^b'(-N(R¹)-COONH₄)₃, HOOC-N (R¹)-R^b-N (R²)-COOH M salt, R^b'(-N(R¹)-COOH)₃M salt, NH₄OOC-OR^cO-COONH₄, HOOC-OR^cO-COOH organic amine M Salt, wherein M are above-described organic amine compound (M).

In this application,⁺MH refers to organic amine M and one or more hydrogen ion (H⁺) it is combined formed cation.

It is preferred that, the second raw material is the one or more in these following compounds：

Oxirane, expoxy propane, epoxychloropropane, epoxy bromopropane, epoxy butane (including various isomers such as 1,2- Epoxy butane, 2,3- epoxy butanes), epoxy chlorobutane (including various isomers such as 1,2- epoxy -4- chlorobutanes, 2,3- epoxies - 1-chlorobutane) or styrene oxide.

It is preferred that, the present invention also provides and prepares wherein A^n-It is any one of (a), (b), (c), (d), (e), (f) or (h) Or the method for the compound of the logical formula (I) of a variety of anion, this method includes：At solvent (preferably protonic solvent or DMF) In, optionally in the presence of catalyst (such as ammoniacal liquor, or organic amine, such as ethamine, diethylamine or triethylamine), by selected from (a) one or more anion and ammonium salt (such as carbamic acid of ammonia formation, in (b), (c), (d), (e), (f) or (h) Ammonium, the aminoquinoxaline replaced on amino by hydroxyalkyl or hydroxyalkyl alkoxy, ammonium carbonate, ammonium formate or ammonium hydrogen carbonate, and The mixture of two or more in them) or the organic amine salt (example that is formed with above-mentioned one or more organic amine compounds (M) Such as carbamic acid organic amine M salt, the carbamic acid organic amine M salt replaced on amino by hydroxyalkyl or hydroxyalkyl alkoxy, carbon Sour organic amine M salt, formic acid organic amine M salt or bicarbonate organic amine M salt, and two or more in them mixture) conduct First raw material, with epoxides described above (such as oxirane, expoxy propane, epoxychloropropane, the ring as the second raw material Oxygen N-Propyl Bromide, epoxy butane (including various isomers such as 1,2- epoxy butanes, 2,3- epoxy butanes), epoxy chlorobutane (including Various isomers such as 1,2- epoxy -4- chlorobutanes, 2,3- epoxies -1-chlorobutane) or styrene oxide, and any two in them Plant or a variety of mixtures) reacted.Or, alternatively, can use includes advance addition and rear neutralization two The method of individual step, i.e. the method for the compound of the logical formula (I) of above-mentioned preparation includes：First, ammonia or above-mentioned one or more have Machine amines (M), with epoxides described above (such as oxirane, expoxy propane, the epoxy chloropropionate as the second raw material Alkane, epoxy bromopropane, epoxy butane (including various isomers such as 1,2- epoxy butanes, 2,3- epoxy butanes), epoxy chlorobutane (including various isomers such as 1,2- epoxy -4- chlorobutanes, 2,3- epoxies -1-chlorobutane) or styrene oxide, and in them Any two or a variety of mixtures) reacted, then, gained compound is with belonging to anion A^n-Presoma respective acids (that is, one or more acid compounds (such as CO2, ammonia of one or more anion in (a)-(g) can be generated Base formic acid, or formic acid) carry out neutralization reaction.It is preferred that, neutralize to pH and be not less than 7.5, more desirably not less than 7.8, it is more preferably not low In 8.

According to the third embodiment the present invention, invention also provides preparation and had as CO₂The moon of donor The method of the orthoformic acid organic amine salt compounds of ion, or prepare wherein A^n-It is the change of the logical formula (I) for the anion that (g) is represented The method of compound, this method includes：Orthoformic acid ester type compound in solvent (preferably protonic solvent, alcohols solvent or DMF), Optionally in the presence of catalyst (such as ammoniacal liquor, or organic amine, such as ethamine, diethylamine or triethylamine), and have belonging to The organic amine M of machine alcamines or with the compound B for belonging to Organic Alcohol amine of at least one above-mentioned N-R group and the presence of water Under reaction is hydrolyzed.Preferably, the amount of the water is sufficient so that at least two ester groups of orthoformic acid ester type compound Hydrolyze, it is further preferred that the amount of water is sufficient so that three ester group hydrolyses of orthoformic acid ester type compound.

It is preferred that, belong to organic amine with least one above-mentioned N-R group (that is, at least one R group bonded with N) Compound B be as the organic amine compound (M) described in ammonia or more and epoxides (such as oxirane, expoxy propane, ring Oxygen chloropropane, epoxy bromopropane, epoxy butane (including various isomers such as 1,2- epoxy butanes, 2,3- epoxy butanes), epoxy Chlorobutane (including various isomers such as 1,2- epoxy -4- chlorobutanes, 2,3- epoxies -1-chlorobutane) or styrene oxide, and Any two or a variety of mixtures in them) reacted prepared by.In the R group, q is average value (i.e. epoxidation The degree of polymerization of thing), as defined above.Preparing wherein A^n-When being the compound of logical formula (I) for the anion that (g) is represented, ammonia Or the mol ratio of organic amine compound (M) and epoxides is preferably 1.3-7, more preferably more preferably 1.5-4,1.5-3.Wherein A^n- It is that compound of the logical formula (I) of (g) is suitable as the polyurethane foamed material that foaming agent is used to prepare heat insulation-type.Namely Say, the present invention also provides and prepares wherein A^n-It is the method for the compound of the logical formula (I) for the anion that (g) is represented, this method includes： Ammonia or above-mentioned one or more organic amine compounds (M), are reacted with the epoxides as the second raw material, and preparing has extremely The organic amine compound B of a few above-mentioned N-R group (that is, at least one R group bonded with N)；Then, orthoformic acid esters Compound is in solvent (preferably protonic solvent, alcohols solvent or DMF), optionally in catalyst (such as ammoniacal liquor, or organic amine Class, such as ethamine, diethylamine or triethylamine) in the presence of, and belonging to the organic amine M of Organic Alcohol amine or with least one Reaction is hydrolyzed in the presence of the compound B and water that belong to Organic Alcohol amine that state N-R groups.Preferably, the water Amount is sufficient so that at least two ester group hydrolyses of orthoformic acid ester type compound, it is further preferred that the amount of water is enough to make Obtain three ester group hydrolyses of orthoformic acid ester type compound.

Preferably, orthoformic acid ester type compound is the one or more in these following compounds：(the C of primitive nail three₁- C₈) alkyl esters, the preferably (C of primitive nail three₁-C₇) alkyl esters, for example, trimethyl orthoformate, triethyl orthoformate, orthoformic acid first Base diethyl ester, tripropyl orthoformate, primitive nail acid methyl dipropyl, tributyl orthoformate, orthoformic acid triphen base ester, orthoformic acid Tribenzyl ester, acetyl group orthoformic acid diethyl ester, acetyl group orthoformic acid ethyl-methyl ester, orthoformic acid binaryglycol ester, orthoformic acid R group in propylene glycol ester, orthoformic acid macrogol ester or orthoformate meets (1a), (2a) or (3a) feature.

It is preferred that, in this application, solvent is selected from following one or more in these：Methanol, ethanol, ethylene glycol, the third two Alcohol, molecular weight be less than 400 polyethylene glycol, molecular weight be less than 300 polypropylene glycol, formamide, glycerine, formic acid glyceride or Water, or DMF.

Obtained according to the 4th embodiment of the present invention there is provided the method by above-mentioned second and the 3rd embodiment Having for obtaining is used as CO₂The organic amine salt compounds of the anion of donor.

According to the 5th embodiment of the present invention there is provided the organic amine salt compound with logical formula (I), and by above-mentioned the What the method for two and the 3rd embodiments was obtained has as CO₂The organic amine salt compounds of the anion of donor, As the purposes of foaming agent, especially as the purposes of polyurethane foams, foamed polystyrene agent or foam polyvinyl chloride agent.On Stating these compounds in this application can foaming agent referred to as of the present invention.

In addition, the invention provides use of the foaming agent of the present invention as foamed polystyrene agent or foam polyvinyl chloride agent On the way, wherein A^n-It is the one or more in following anion：

(a)R¹R²N-COO^-；Wherein R¹And R²It is hydrogen, methyl, ethyl, H (OCH independently of one another₂CH₂)_q-、H(OCH₂CH (CH₃))_q-、H(OCH(CH₃)CH₂)_q-、H(OCH₂CH(C₆H₅))_q-、H(OCH(C₆H₅)CH₂)q-、H(OCH₂CH(CH₂Cl))_q-、H (OCH(CH₂Cl)CH₂)_q- or H (OCH₂CH(CBr₃))_q-；

(b)CO₃ ^2-；Or

(d)HO-COO^-。

In addition, in view of the decomposition temperature of ammonium formate (116 DEG C of fusing point) or formic acid organic amine M salt is higher, it is conventionally believed that They are not suitable for polyurethane foam.But, present inventor is by substantial amounts of research work it was unexpectedly observed that working as first Sour ammonium (116 DEG C of fusing point) or formic acid organic amine M salt can generate unstable with NCO group reaction when touching isocyanate groups Acid anhydrides, then decomposes to give off rapidly carbon dioxide and carbon monoxide.

In this application, when preparing logical formula (I) compound using ammonium formate and epoxides, it is preferred that first by Formic acid carries out reaction with ammoniacal liquor and obtains formic acid aqueous ammonium, then adds a small amount of organic amine (such as methylamine, dimethylamine or front three Amine, ethylamine or diethylamide), thermal dehydration or it is concentrated under reduced pressure or is concentrated in vacuo (such as so that water content is 7-15wt% is Only, such as 10wt% or so), then pass to epoxides (such as oxirane and/or expoxy propane) and reacted, obtain formic acid Alcohol amine salt (I).Here, the addition of a small amount of organic amine (such as methylamine, dimethylamine or trimethylamine, ethylamine or diethylamide), Enable to prevent when formic acid alcohol amine salt (I) is used for and prepares composition, foam (" white material ") in composition, foam (" white material ") hair Raw crystallization, deposited phenomenon.

In this application, logical formula (I) chemical combination is prepared when ammonium hydrogencarbonate is reacted as the first raw material and the second raw material During thing, usable catalyst, such as methylamine, dimethylamine, alcamines, other amines catalysts, bimetallic catalyst class (class), or Using pressurized, heated.

In addition, by selected from least one of these following alcamine compounds alcohol amine compound, (they are that have extremely Few N-H organic amine compound (M))：

C₂-C₁₂Alcamines, such as monoethanolamine, diethanol amine, triethanolamine, monopropylene glycol amine, dipropanolamine, three propyl alcohol Amine, monoisopropanolamine, diisopropanolamine (DIPA), triisopropanolamine, monobutanolamine, two butanolamines, or three butanolamines,

With belonging to anion A^n-The respective acids of presoma neutralized the organic amine salt of formed below general formula (Ia) Compound

A^n-[B^m+]_p (Ia)

Also can be directly as foaming agent, especially as polyurethane foams, foamed polystyrene agent or foam polyvinyl chloride Agent.These above-mentioned compounds in this application can foaming agent referred to as of the present invention.Polyurethane foams or for polyurethane foam In composition.Certainly, these compound blowing agents of formula (Ia) are not preferred, because it or they pH value is typically low In 8, even below 7.5, more even below 7.1.When the polyurethane foamed material for preparing heat insulation-type, especially obturator-type During polyurethane foamed material, from bubbling efficiency, the smell of foaming agent, heat-insulating property and abscess-size stability and polyurethane foam The dimensional stability of foam body considers, these organic amine salt compounds (Ia) (be not on the spot (in situ) by organic amine Compound (M) with prepared by epoxide reaction) be not preferred.

In addition, present inventor is it was unexpectedly observed that the compatibility of ammonium formate and polymer polyatomic alcohol is relatively good, i.e. first Sour ammonium can be directly dissolved in polymer polyatomic alcohol, therefore ammonium formate can be directly used as polyurethane foams, therefore, the application Ammonium formate is additionally provided as the purposes of foaming agent, especially as polyurethane foams.When in ammonium formate containing it is a small amount of (for example 0.5-8wt%, such as 1-6wt%) organic amine such as methylamine, dimethylamine, trimethylamine or monoethanolamine when, formic acid aqueous ammonium is not Generation crystallization, precipitation.

Foaming agent of the present invention (that is, lead to the compound of formula (I), or by the method for above-mentioned second or the 3rd embodiment What is obtained has as CO₂The organic amine salt compounds of the anion of donor) there are following characteristics：1) not in addition or not In the case of extra addition alkali compounds, the pH value of foaming agent of the present invention is in 7.5-10, it is preferable that be pH 7.8-9.5, more excellent Select between pH 8-9；2) content of alkali metal or alkaline-earth metal be 0-200ppm (quality), preferably shorter than 150ppm, it is more preferably low It is optimal in 100ppm, more preferably less than more preferably less than 50ppm, more preferably less than 20ppm, more preferably less than 10ppm, 5ppm Elect as less than detectable limit or for 0ppm；3) content of water or the content of the water existed as solvent are 0-40wt%, preferably 5-35wt%, more preferably 10-30wt%, more preferably 15-25wt%；4) heat decomposition temperature is between 36-120 DEG C and divided CO is discharged during solution₂Gas；The wherein higher certain form of foaming agent thing of the present invention of decomposition temperature is when touching NCO group Become less stable, can be decomposed between 45-70 DEG C and discharge CO₂；5) it is preferably, each molecule of foaming agent of the present invention Containing at least one R group, the R group is, for example, HOCH₂CH₂-、HOCH₂CH(CH₃)-、HOCH(CH₃)CH₂-、HOCH₂CH (C₆H₅)-、HOCH(C₆H₅)CH₂-、HOCH₂CH(CH₂Cl)-、HOCH(CH₂Cl)CH₂-、HOCH₂CH(CBr₃)-or HOCH (CBr₃) CH₂-；Further preferably, foaming agent of the present invention has the compound of logical formula (I) simultaneously comprising a variety of (preferred 2-5 kinds, such as 2 or 3 kind) And average per molecule contains 1.5-5 R group, the R group is, for example, HOCH₂CH₂-、HOCH₂CH(CH₃)-、HOCH(CH₃) CH₂-、HOCH₂CH(C₆H₅)-、HOCH(C₆H₅)CH₂-、HOCH₂CH(CH₂Cl)-、HOCH(CH₂Cl)CH₂-、HOCH₂CH(CBr₃)- Or HOCH (CBr₃)CH₂-；6) it is 30-100%, preferably 50%-100% among all N atoms in foaming agent of the present invention, more excellent Select 70%-100%, more preferably 85%-100% that there is N-H covalent bonds；7) in foaming agent of the present invention, lead to formula (I) compound and The total content of water is the 70-100% based on gross weight, is more typically 80-99.999%, is more typically 85-99.0% (containing molten Agent, and allow containing a small amount of nonmetallic inclusion)；8th, with infrared spectrum analysis, some foaming agents of the present invention have in 2932- 2970cm^-1The secondary amine salt N-H of scope stretching vibration is unimodal, in 1555-1566cm^-1The secondary amine salt N-H of scope flexural vibrations It is unimodal, in addition, in 3200-3400cm^-1The OH stretching vibration peaks of the strong and wide Hydrogenbond of scope, show both had in foaming agent There is hydroxyl, secondary amine contains water simultaneously.Therefore, foaming agent of the present invention includes one or more alcohol amine compounds and typically contained There is water.

It is further preferred that the compound average per molecule of logical formula (I) contains 1.5-5 R group.

According to the 6th embodiment of the present invention, the present invention also provides polyurethane foamed composite thing, and it is included：0.01- 100 weight % above-described logical formula (I) compound (or is obtained by the method for above-mentioned second and the 3rd embodiment Have be used as CO₂The organic amine salt compounds of the anion of donor)；0-50 weight % physical blowing agent；0-5 weight % Water, and 0.0-99.99 weight % polymer polyatomic alcohol；Wherein, the percentage by weight is based on polyurethane foamed composite thing Gross weight.It is preferred that, it is included：0.1-80 weight % (more preferably 1-70wt%, more preferably 3-60wt%, more preferably 5- 50wt%, more preferably 7-40wt%, such as 10wt%, 15wt%) above-described logical formula (I) compound；0-40 weight %'s Physical blowing agent；0-4 weight % water, and 20.0-99.9 weight % (more preferably 30-99wt%, more preferably 40-97wt%, more It is preferred that 50-95wt%, more preferably 60-93wt%, such as 90wt% or 85wt%) polymer polyatomic alcohol；Wherein, the weight hundred Divide gross weight of the ratio based on polyurethane foamed composite thing.Preferably, composition, foam of the invention contains 0.5-4wt% altogether Water, more preferably 0.8-2.5wt%, more preferably 1-2.2wt% water.

It is preferred that, described composition, foam is further included：Foam stabiliser, catalyst and fire retardant etc..These auxiliary agents It is to commonly use in polyurethane field.

It is preferred that, polymer polyatomic alcohol is selected from：PPG, PEPA, polyether-polyester polyol, makrolon Glycol, polycarbonate-polyester polyalcohol, makrolon-PPG, polybutadiene polyol or polysiloxane polyhydric alcohol. The average functionality of polymer polyatomic alcohol is generally 2-16, more preferably preferably 2.5-10,3-8.

At least one of it is preferred that, the physical blowing agent is selected from the group：Pentane, isopentane, pentamethylene, boiling point is in 0- Other alkane in the range of 100 DEG C, HCFC-141b, HFC-245fa, HFC-365mfc, LBA, FEA-1100, boiling point is in 0-100 Other fluorochlorohydrocarbons in the range of DEG C, methyl formate.

Typically, composition, foam of the invention is transparent or clarification.This shows foaming agent dissolving or uniform of the present invention It is dispersed in polymer polyatomic alcohol.

The polyurethane foamed composite thing (being commonly called as " white material ") of the present invention has following characteristics：1st, comprising alcohol amine salt or alcohol amination Compound is (for example, the compound of logical formula (I) discharges CO after pyrolysis₂, while remaining alcamine compound)；2nd, it is transparent or clear Clearly；3rd, discharged in the case where heating (such as 40-80 DEG C of temperature) or in the case of addition sour (inorganic acid or organic acid) Go out CO₂, peak decomposition temperature is usually between 45-65 DEG C；4th, when composition, foam (i.e. " white material ") and isocyanates or many When isocyanates (such as MDI or TDI) is contacted or mixed, the material moment (such as 0.2-4 seconds, such as 1-2 seconds) of mixing turns milky white Color.In the present invention, material becomes rapidly milky, with volume rapid expanding phenomenon, but this process and non-foam real rises Hair, material just starts to rise afterwards.Comparatively, using water, or during using water and physical blowing agent as foaming agent, foam breast It is white and to rise be while carrying out and being all delay.

Although in the present invention, composition, foam (" white material ") can include a small amount of water as blowing promotor, due to The logical formula (I) compound of the present invention preferentially decomposes release CO₂, i.e., preferential foaming, therefore, the addition of a small amount of water does not influence to foam Journey does not influence polyurethane foam end properties.

When including wherein A in the polyurethane foamed composite thing (be commonly called as " white material ") of the present invention^n-It is (f) HCOO^-(formate) Logical formula (I) compound when, it is preferred that polyurethane foamed composite thing of the invention (being commonly called as " white material ") is comprising 1-5 weight Water.Purpose is to reduce the amount of the carbon monoxide (CO) discharged in foaming process.

The present invention also provides polyurethane foamed material, and it passes through above-described polyurethane foamed composite thing and polyisocyanic acid Ester monomer (such as MDI or TDI) or isocyanate-terminated prepolymer react and formed after being mixed.Typically, it is described poly- The weight ratio of urethane composition, foam and polyisocynate monomer or isocyanate-terminated prepolymer is, such as 0.5:1-2: In the range of 1, preferably 0.5:1-1:In the range of 1.It is preferred that, described weight than should cause the reactive hydrogen of composition, foam with The equivalent proportion of contained-NCO group is 0.6-1.2 in polyisocynate monomer or isocyanate-terminated prepolymer:1, more preferably 0.7-0.9:1, i.e. NCO are slightly excessive relative to reactive hydrogen.

The present invention also provides the purposes of polyurethane foamed material, and it is used for polyurethane coating, refrigerator and refrigerator-freezer insulation, packaging Case insulation, insulating board for building, color steel, cold storage plate, the insulation of pipeline, LNG conveying insulations etc..

It is preferred that, leading to the organic amine salt compound of formula (I) has at least two reactive hydrogens, such as 2-10, preferably 3-6. The reactive hydrogen is present in the form of primary amine groups, secondary amine or hydroxyl.Therefore, the organic amine salt compound for leading to formula (I) can Enough discharge CO₂To participate in foaming, chain extension and/or crosslinking are participated in again, strengthen intensity (the i.e. mechanical strength and/or machinery of abscess Intensity) so that the polyurethane foam obtained has good dimensional stability.Especially, when the density of polyurethane foam< 25kg/m³When, the polyurethane foam obtained with the foaming agent of prior art has serious shrinkage phenomenon, still, is sent out with this The polyurethane foam that bright logical formula (I) compound is obtained as foaming agent then has excellent dimensional stability, especially exists Almost without macroscopic shrinkage phenomenon in the case of the time for placing at least five month under environmental condition or room temperature condition.Example Such as, according to chinese national standard GB/T 8811-2008, simply standing time change, the finished foam material for preparing of the present invention (density<25kg/m³) placed 5 months under the conditions of room temperature (23 ± 2 DEG C), (length dimension becomes the shrinkage factor of polyurethane foam Rate ε_LOr width dimensions rate of change ε_wOr thickness rate of change ε_r) be generally below 7%, more preferably less than 5%, it is further excellent Choosing is less than 3%, even more preferably less than 1%.The rate of closed hole of polyurethane foam of the present invention is usually>95%, more preferably> 96%, more preferably 97%, more preferably 98%.

The organic amine salt compound of the logical formula (I) of the present invention, can be according to each of polyurethane foamed material to be prepared Application field is planted specifically to be designed.

For example, being used as refrigerator, refrigerator, frozen products insulated container when the composition, foam (being commonly called as " white material ") of the present invention is used to prepare Or the heat-insulating material of refrigerator car polyurethane foamed material when, prepare wherein A^n-It is the change of (a)-(f) or (h) logical formula (I) In the reaction of compound, the mol ratio of the first raw material and the second raw material is usually 1:1.3-3.5, preferably 1:1.5-3.In addition, working as When the composition, foam (being commonly called as " white material ") of the present invention is used for spraying application, the mol ratio of the first raw material and the second raw material is usually 1:2.8-5, preferably 1:3-4.5, more preferably 1:3.3-4.

Preferably, the reaction temperature for preparing logical formula (I) compound be between 0-200 DEG C, such as 10 DEG C, 20 DEG C, 30 DEG C, 40℃、50℃、60℃、70℃、80℃、90℃、100℃、110℃、120℃、130℃、130℃、150℃、160℃、170 DEG C, 180 DEG C and 190 DEG C.The pressure of reaction is such as 0.3MPa, 0.6MPa, 0.9MPa and 1.2MPa between 0.1-1.5MPa. Reaction time is such as 0.5 hour between 0.5-20 hours, 1 hour, 2 hours, 3 hours, 4 hours, 5 hours, 6 hours, it is 7 small When, 8 hours, 9 hours, 10 hours, 11 hours, 12 hours, 13 hours, 14 hours, 15 hours.

The decomposition temperature of the logical formula (I) compound of the present invention is usually between 45-120 DEG C, between preferably 50-70 DEG C, Or, when touching isocyanates, its decomposition temperature is between 45-70 DEG C.

The advantageous effects or advantage of the present invention

1st, logical formula (I) compound or foaming agent of the present invention of the invention have suitable decomposition temperature, or different when touching There is suitable decomposition temperature during cyanate, on the one hand store stable at room temperature, on the other hand during polyurethane foam Can be with rational speed carbon dioxide gas, to cause expanded material has preferable when foamable reaction system heats up The distribution density of performance, such as abscess, the dimensional homogeneity of abscess.

2nd, logical formula (I) compound of the invention has solubilizing group i.e. R group, and the compound (I) can be with molecular level Equably dissolve or be distributed in polymer polyatomic alcohol such as PPG and/or PEPA, or polyvinyl chloride (PVC) resin Or in polystyrene (PS) resin, it is ensured that the uniformity of foaming, it is to avoid local excessive foams.

3rd, logical formula (I) compound of the invention has hydramine residue or with alcohol amine compound, is decomposed in the foaming agent (I) Discharge CO₂Catabolite produced afterwards is that alcohol amine compound still contains at least two reactive hydrogens, and they are suitable as Chain extender and/or crosslinking agent, logical formula (I) compound of the invention not only as " blow point " but also were used as " chain extension point " and/or " were crosslinked Point ", significantly enhances the mechanical strength and mechanical strength of abscess, and the polyurethane foam obtained has good dimensionally stable Property, shrinkage phenomenon is almost not observed in polyurethane foam finished product naked eyes after some months, even 1 year is placed, without the bubble that collapses Or collapse phenomenon.The long period such as (10 days) is placed especially at higher temperature (such as 40-60 DEG C) afterwards still with good Good dimensional stability.

4th, logical formula (I) compound of the invention is not allowed volatile, and (metal ion does not have corruption to metal ion to metal base Corrosion), and chlorofluorocarbon blowing agent is wholly or largely substituted, therefore, have great importance for environmental protection, and And the effect of foaming is substantially better than foaming effect when using other foaming agents in the prior art.

5th, when being mixed with pentamethylene as foaming agent, compared with pentamethylene is used alone, foam material can be significantly improved The heat-insulating property of material.When being used as foaming agent with CFC such as HCFC-141b, HFC-245fa or HFC-365mfc mixing, with list Solely compared using CFC, the heat-insulating property of foamed material can be significantly improved.At present, foaming agent or specific chlorine are generally surrounded Fluorocarbon blowing agents come select to related foaming agent intersolubility or the preferable special polyether polyalcohol of compatibility, and use the present invention Foaming agent, without selecting specific PPG or PEPA, usage range extensively, can make in composition, foam With various types of PEPAs and/or PPG.

6th, foaming agent of the invention has amido, and itself has self-catalysis function, can reduce polyurethane foaming catalyst Use, can at least reduce the use of early stage catalyst or can even save early stage catalyst.

7th, compared with prior art, the polyurethane foams that provides of the present invention not chlorofluorocarbon, ODP (is broken to ozone layer Bad latent energy value) it is equal to 1 for 0, GWP (chamber effect potential value), it is most environmentally friendly polyurethane foams, performance comparision is excellent, Cryogenic property is extremely excellent, after testing the existing best physical blowing agent of the thermal conductivity ratio in the case of subzero 160 degrees Celsius Low by 20% or so, this excellent characteristic can be used for the insulation of natural gas long-distance transportation pipeline, and another characteristic is and pentamethylene The thermal conductivity factor of foamed material can be greatly lowered by being used in mixed way, and refrigerator can be greatly lowered in this excellent heat-insulating property The power consumption of the equipment such as refrigerator-freezer.The alternative existing all physical blowing agents containing halocarbon of polyurethane foams that the present invention is provided, Meet the production application of polyurethane material.

8th, with the size of foaming agent of the present invention or logical formula (I) compound as the polyurethane foamed material prepared by foaming agent Rate of change or shrinkage factor≤4.5%, preferably≤1.5%, more preferably≤0.5% (according to chinese national standard GB/T 8811- 2008, standing time can be according to required in the standard, or even, standing time is 5 months).In addition, for example in 34-42Kg/ m³Density foam under, thermal conductivity factor w/mk (10 DEG C) or w/mk (22.5 DEG C) be between 0.01900-0.02200, Preferably between 0.01910-0.02150.And thermal conductivity factor of the polyurethane foam of prior art under this density is general Higher than 0.02200, more generally higher than 0.02300.In addition, in this density range, the compressive strength of foams of the present invention is In 110-220Kpa scopes, preferably 150-200Kpa scopes.

Brief description of the drawings

Fig. 1 is the infrared spectrogram of embodiment A-3 product.

Fig. 2 is the infrared spectrogram of embodiment A-4 product.

Fig. 3 is the infrared spectrogram of embodiment B-6 product.

Fig. 4 is the electron scanning micrograph (SEM) of the foams of embodiment 4.

Fig. 5 is the SEM for the contrast foams 4-1 for repeating embodiment 4.

Fig. 6 is the SEM for the reference foams 4-2 for repeating embodiment 4.

Fig. 7 is the SEM for the contrast foams 4-3 for repeating embodiment 4.

Fig. 8 is the SEM for the reference foams 4-4 for repeating embodiment 4.

Fig. 9 is the SEM of the foams of embodiment 16.

Figure 10, Figure 12 and Figure 14 are the outward appearance of use compound A-4 of the invention as the polyurethane foam of foaming agent Photo.

Figure 11, Figure 13 and Figure 15 are the outward appearance photo of the contrast polyurethane foam with Water blown.

Figure 16 is the SEM of the polystyrene foamed material of embodiment 34.

Embodiment

With reference to embodiment, the present invention will be further described.

In this application, for preparing polyurethane foam or for the conventional PPG in composition, foam and poly- Ester polyol is selected from following kinds：Polyethers 4110,450,400A, MN500, SU380, SA380,403, SA460, G350；Polyester CF6320、DM2003、YD6004、AKS7004、CF6255.Custom catalystses are selected from：33LV(A-33)：33% triethylene diamine DPG solution, N, N- dimethylethanolamines, N, N- dimethyl benzylamines, the dipropyl two of 70% pair of (dimethylamino ethyl) ether Alcoholic solution, 70% potassium octanoate are in diethylene glycol solution, dibutyl tin laurate, PT303, PT304, potassium acetate, PC-8 (N, N- Dimethyl cyclohexyl amine), PC-5, PC-41, triethanolamine, JXP-508, JXP-509, TMR-2, TMR-3, TMR-4.It is conventional fire-retardant Agent：TCPP, TCEP, DMMP, ammonium chloride, aluminium-hydroxide powder, DM1201, DM1301, tetrabromo-benzene anhydride diol.Conventional silane surfaces Activating agent：DC8545、AK-158、AK-8805、AK-8812、AK-8809、AK-8818、AK-8860、DCI990、DC5188、 DC6070、DC3042、DC3201.Non- silane surface active agent：LK-221,LK-443.

Safety instruction：The situation for being directed to use with epoxide every in the present invention, for the sake of security, will react Thing has to pass through before and after adding reactor to be reacted under inert gas (such as nitrogen or argon gas) processing and protection, is prevented Blast.In addition, when adding oxirane, for the sake of security, be preferably added portionwise in reactor, and epoxy Propane can be added disposably in reactor, can also be in batches.Reactor is generally the pressure reactor equipped with cooling device, removes It is non-to be otherwise noted.

According to chinese national standard GB/T 26689-2011, (refrigerator, refrigerator-freezer are moulded with hard polyurethane foams in embodiment Material) test foams properties.The size of sample is generally 10*10*2.5cm.

Thermal conductivity factor is carried out according to GB/T 10294-2008 or GB/T 10295-2008.Mean temperature is 10 DEG C, cold and hot 15~20 DEG C of the plate temperature difference.Apparent (core) density is tested according to GB/T 6343-2009.Low-Temperature Size stability is according to GB/T 8811-2008, is tested at -30 DEG C ± 2 DEG C.Compressive strength is tested according to GB/T 8813-2008.Rate of closed hole (i.e. closed pore Percentage by volume) tested according to GB/T 10799-2008.

A) logical formula (I) compound is prepared from amino acid ammonium salt or carbamic acid organic amine (M) salt

Embodiment A-1

1.4 tons of aminoquinoxalines (molecular weight 78.07), 0.7 ton of ethylene glycol, 0.9 ton of water are added to cold But in the stainless steel autoclave (the abbreviation reactor in following other embodiments) of water leg, agitator is started so that Aminoquinoxaline slowly dissolves and (is not necessarily completely dissolved), uses nitrogen purge, then closed reactor and starts stirring, 1.7 tons altogether of expoxy propane (molecular weight 58.08,34 DEG C of boiling point) is passed through, controls the charging rate of expoxy propane to control Pressure in reactor is not higher than 0.6MPa, is slowly heated up in the case where being stirred continuously, and temperature control reacts 15 hours below 70 DEG C, reaction Complete, slowly reduce the temperature to after 50 DEG C and control vacuum (preferably shorter than 500mmHg) below 600 millimetress of mercury slowly to remove Unnecessary water (for example reaching the water content less than 20wt%), then bleeds off vacuum, cools to and reaction is released after less than 40 DEG C Thing, obtains compound A-1.The centipoise of viscosity 200, pH=9, compound A-1 decomposition temperature is 45-70 DEG C of (since 45 DEG C pole It is slowly decomposed, and peak decomposition temperature is 57-62 DEG C).With atomic absorption spectrophotometer (Seiko Instruments, Inc.；SAS/727 the content for) determining alkali and alkaline earth metal ions ion is less than detectable limit.

Compound A-1 is a kind of at room temperature or in the more stable transparent or supernatant liquid of environmental condition, is suitable as Polyurethane foams, it and HFC-245fa, LBA, the fundamental characteristics of 3-pentafluorobutane contrast such as following table：

	Compound A-1	HFC245fa	3-pentafluorobutane	LBA
					ODP	0	0	0	0
GWP	1	1030.01	793.98	5.00
					Boiling point (DEG C)	45 DEG C start slow decompose	15.3	40.2	19.3

As can be seen from the above table, compound A-1 GWP (chamber effect potential value) is equal to 1, and decomposition temperature is higher, gram Many shortcomings of some low boilings (being less than 20 DEG C) physical blowing agent such as HFC-245fa, LBA, 3-pentafluorobutane etc. are taken, such as GWP is much larger than 1, boiling point than relatively low, volatile, and to be equal to 1, boiling point higher, not volatile by the compounds of this invention A-1 GWP, And ODP (to latent energy value of the destruction of ozone layer) is 0, will not destroy atmospheric ozone layer；It is not volatile to be readily transported and store.

Embodiment A-2

1.4 tons of aminoquinoxaline, 0.7 ton of ethylene glycol, 0.9 ton of water are added to the stainless steel with cooling jacket In reactor, start stirring so that aminoquinoxaline slowly dissolves and (is not necessarily completely dissolved), reaction system through nitrogen treatment and Heat temperature raising after protection, it is 45-70 DEG C to control temperature, and control pressure is no more than 0.6MPa, is then slowly added in batches total The oxirane (molecular weight 44.05) of 1.3 tons of meter, controls 45-70 DEG C of temperature, pressure is in 0.6MPa reactions stirred below after adding 5 hours, 50 DEG C are then cooled to, the unnecessary water of lower removing is depressurized under 600mHg and (for example reaches that the water less than 30wt% contains Amount), cool to and product is released after less than 40 DEG C, obtain compound A-2.Viscosity about 250, pH=9, compound A-2 decomposition Temperature is in 45-70 DEG C of scope.

Embodiment A-3 (present invention is preferably)

1kg aminoquinoxaline, 1kg water are added in reactor, dissolving under agitation (allows to exist undissolved Aminoquinoxaline), 2kg expoxy propane is then added into transparent quartz glass reactor, is started stirring, is being stirred continuously Under slowly heat up, temperature control is between 50-60 DEG C, and pressure is reacted under the conditions of being not higher than 0.6MPa, when reaction proceeds to about 2 Marvellous phenomenon is occurred in that suddenly during hour：Muddy, opaque mixture moment becomes transparent or clear solution, continues to react 8 hours, 50 DEG C are then cooled to, is that below 600 millimetress of mercury deviate from unnecessary water in vacuum, cools to after less than 40 DEG C Release product.Reaction time ensures that reaction is completed according to mol ratio.Obtain compound A-3.The centipoise of viscosity 200, pH=9.1, point Temperature is solved in 45-70 DEG C of scope.Liquid-phase chromatographic analysis and gas chromatographic analysis, show that compound A-3 includes a variety of hydramine Mixture.Water content is 21.5wt%.Infrared spectrogram is as shown in Figure 1.

Embodiment A-4 (present invention is preferably)

1 ton of aminoquinoxaline, 1 ton of water are added in the stainless steel pressure reactor with cooling water jecket, The lower dissolving (allowing the presence of undissolved aminoquinoxaline) of stirring, uses nitrogen purge, 2.2 tons of ring is then added portionwise Ethylene Oxide is into reactor, and then closed reactor, starts stirring, slowly heated up in the case where being stirred continuously, temperature control 45-70 DEG C it Between, pressure reacts 10 hours under the conditions of being not higher than 0.6MPa, then cools to 50 DEG C, is below 600 millimetress of mercury in vacuum The unnecessary water of abjection, cools to and product is released after less than 40 DEG C.Obtain compound A-4.The centipoise of viscosity 200, pH=9 is decomposed Temperature is in 45-70 DEG C of scope.Liquid-phase chromatographic analysis and gas chromatographic analysis, it is to include a variety of hydramine to show compound A-4 Mixture.Infrared spectrogram is as shown in Figure 2.

Embodiment A-5 (present invention is preferably)

7kg ammonium carbonate and 7kg aminoquinoxaline, 12kg water are added in reactor, dissolving under agitation (is permitted Permitted the presence of undissolved aminoquinoxaline and ammonium carbonate), 30kg expoxy propane is then added portionwise again, it is lower slow being stirred continuously Slow heating, temperature control is between 45-70 DEG C, and control pressure is not higher than 0.6MPa, reacts 10 hours, then cools to 50 DEG C, temperature control Below 50 DEG C, vacuum is to deviate from unnecessary water below 600 millimetress of mercury, cools to and vacuum is bled off after less than 40 DEG C, is put Go out product, that is, obtain compound A-5.The centipoise of viscosity about 200, pH=9, decomposition temperature is in 45-70 DEG C of scope.

Embodiment A-6 (present invention is preferably)

16kg carbamic acid monoethanolamine salt, 10kg water are added in reactor, nitrogen purge reactor is used, stirs Dissolving is mixed, 12kg expoxy propane is added portionwise into reactor, stirring is started, control pressure is not higher than 0.6MPa, continuous Slowly heated up under stirring, when temperature control reaction 5 is small when temperature is increased to 70 DEG C, then reduce the temperature to less than 50 DEG C, control is true Unnecessary water is removed below the millimetres of mercury of reciprocal of duty cycle 600, cools to and vacuum is bled off after less than 40 DEG C, product is released, you can obtain Compound A-6.The centipoise of viscosity 230.PH=9.Decomposition temperature is in 45-70 DEG C of scope.

Embodiment A-7

20kg carbamic acid diethylenetriamines salt, 10kg water are added in reactor, stirring and dissolving, in stirring Under, control pressure is not higher than 0.6MPa, and 15kg expoxy propane is added portionwise into reactor between 45-70 DEG C in temperature, plus Temperature control is reacted 5 hours after complete expoxy propane, then cools at 50 DEG C, and vacuum is removed under being depressurized below 600 millimetress of mercury Unnecessary water, cool to bled off after less than 40 DEG C vacuum, release product can obtain compound A-7.About 350 lis of viscosity Pool.PH=9, decomposition temperature is in 45-70 DEG C of scope.

Embodiment A-8

1 ton of aminoquinoxaline (molecular weight 78.07), 1 ton of water are added in reactor, dissolving under agitation (is permitted Permitted the presence of undissolved aminoquinoxaline), then add 2.8 tons of epoxychloropropane (that is, chloro- 1,2- epoxies of epichlorohydrin or 3- Propane, molecular weight 92.52,117.9 DEG C of boiling point) into reactor, stirring is started, is slowly heated up in the case where being stirred continuously, temperature control exists Between 45-70 DEG C, pressure reacts 10 hours under the conditions of being not higher than 0.6MPa, then cools to 50 DEG C, is 600 millimeters in vacuum Deviate from unnecessary water below mercury column, cool to and product is released after less than 40 DEG C.Obtain compound A-8.The centipoise of viscosity 450, pH =9, decomposition temperature is in 45-70 DEG C of scope.

Embodiment A-9

0.65 ton of ammonium carbonate and 0.65 ton of aminoquinoxaline, 1.2 tons of water are added in reactor, under agitation Dissolve (allowing the presence of undissolved aminoquinoxaline and ammonium carbonate), then add 3.6 tons of styrene oxide (styrene oxide, molecular weight 120.15), slowly heats up in the case where being stirred continuously, and temperature control is between 45-70 DEG C, control pressure Not higher than 0.6MPa, reacts 10 hours, then cools to 50 DEG C, and temperature control is below 50 DEG C, and vacuum is below 600 millimetress of mercury The unnecessary water of abjection, cools to and vacuum is bled off after less than 40 DEG C, product is released, that is, obtain compound A-9.Viscosity about 460 Centipoise, pH=9, decomposition temperature is in 45-70 DEG C of scope.

B) preparing has CO₃ ^2-The logical formula (I) compound of anion

Embodiment B-1

14kg ammonium carbonate (molecular weight 96), 6kg ethylene glycol and 8kg water are added in reactor, stirring is started, So that ammonium carbonate slowly dissolves and (is not necessarily completely dissolved), 20kg expoxy propane is added, stirring is started, control pressure is not higher than 0.6MPa, is slowly heated up in the case where being stirred continuously, and temperature control reacts 12 hours below 70 DEG C, and reaction is completed, and is slowly reduced the temperature to After 50 DEG C control vacuum unnecessary water is slowly removed below 600 millimetress of mercury, then bleed off vacuum, cool to 40 DEG C with Reactant is released after lower, compound is obtained and obtains compound B-1.The centipoise of viscosity about 300, pH=9, compound B-1 decomposition Temperature is 45-70 DEG C.Liquid-phase chromatographic analysis and gas chromatographic analysis, it is the mixing for including a variety of hydramine to show compound B-1 Thing.With atomic absorption spectrophotometer (Seiko Instruments, Inc.；SAS/727) determine alkali and alkaline earth metal ions from The content of son is less than detectable limit.

Embodiment B-2

1.4 tons of ammonium carbonate, 1 ton of water are added in the stainless steel pressure reactor with cooling jacket, stirred molten Solve (allowing the presence of undissolved ammonium carbonate), purged with nitrogen, then seal reactor, in the case where being stirred continuously, control temperature exists Between 45-70 DEG C, control pressure is not higher than 0.6MPa, and 1.3 tons of oxirane is added portionwise in reactor, is controlled after adding Temperature reaction 4 hours, then cools to 50 DEG C, control vacuum removes unnecessary water under below 600mHg decompressions, cools to 40 Vacuum is bled off after below DEG C, product is released.Obtain compound B-2.The centipoise of viscosity 300.PH=9.1.Decomposition temperature is in 45- 70℃.Liquid-phase chromatographic analysis and gas chromatographic analysis, it is the mixture for including a variety of hydramine to show compound B-2.

Embodiment B-3

The water of 20kg ammonium carbonate, 18kg is added in transparent quartz glass reactor, stirring and dissolving (allows to exist Undissolved ammonium carbonate), in the case where being stirred continuously, control temperature is between 45-70 DEG C, and control pressure is not higher than 0.6MPa, will 45kg expoxy propane is added in reactor, adds the reaction of rear temperature control, when reaction proceed to about 2 it is small when or so when go out suddenly Marvellous phenomenon is showed：Muddy, opaque mixture moment becomes transparent or clear solution, continues to react 8 hours, then drops Temperature is to 50 DEG C, and control vacuum removes unnecessary water under below 600mHg decompressions, cools to and vacuum is bled off after less than 40 DEG C, is put Go out product.Obtain compound B-3.Viscosity is about 250 centipoises.PH=9.1.Decomposition temperature is at 45-70 DEG C.

Embodiment B-4

20kg ammoniacal liquor (concentration 25wt%) is added in reactor, stirring is started, control pressure is not higher than 0.6MPa, Temperature is no more than 120 DEG C, and 16kg oxirane is added portionwise, and adds rear temperature control and reacts 1 hour.Room is cooled to after the completion of reaction Remove unnecessary water after temperature under reduced pressure, it is 8 or so to be passed through 4kg carbon dioxide (molecular weight 44) to pH value, temperature control 80 DEG C with Under, room temperature is cooled to after the completion of reaction.Obtain compound B-4.Viscosity is about 400 centipoises.Decomposition temperature is at 45-75 DEG C Scope.

Embodiment B-5

20kg ammoniacal liquor (concentration 25wt%), 5kg ethylene glycol are added in reactor, stirring, control pressure is started Not higher than 0.6MPa, temperature is no more than 120 DEG C, and 20kg expoxy propane is added portionwise, and adds rear temperature control and reacts 2 hours.Reaction After the completion of cool to after room temperature and remove unnecessary water under reduced pressure, carbon dioxide to the pH value for being passed through 5kg is 8 or so, and temperature control is 80 Below DEG C, room temperature is cooled to after the completion of reaction.Obtain compound B-5.Viscosity is about 450 centipoises.Decomposition temperature is in 45- 75 DEG C of scopes.

Embodiment B-6

The diethylenetriamine (molecular weight 103.17) of 10kg parts by weight, 15kg water are added in reactor, started Stirring, control pressure is not higher than 0.6MPa, and temperature is no more than 120 DEG C, 15kg expoxy propane is added portionwise, rear temperature control is added anti- Answer 1 hour.Cooled to after the completion of reaction and remove unnecessary water after room temperature under reduced pressure, carbon dioxide to the pH value for being passed through 6kg is 8 left The right side, temperature control cools to room temperature below 80 DEG C after the completion of reaction.Obtain compound B-6.Viscosity is about 500 centipoises.Point Temperature is solved in 45-70 DEG C of scope.Infrared spectrum is as shown in Figure 3.

Embodiment B-7

10kg ethylenediamine (molecular weight 60.12), 15kg water are added in reactor, stirring, control pressure is started Not higher than 0.6MPa, temperature is no more than 120 DEG C, and 10kg oxirane (molecular weight 44.05) is added portionwise, rear temperature control is added anti- Answer 1 hour.Cooled to after the completion of reaction and remove unnecessary water after room temperature under reduced pressure, carbon dioxide to the pH value for being passed through 5kg is 8 to be Only, temperature control cools to room temperature below 80 DEG C after the completion of reaction.Obtain compound B-7.Viscosity is about 500 centipoises.Point Temperature is solved in 45-70 DEG C of scope.

C) preparing has formate (HCOO^-) logical formula (I) compound

Embodiment C-1

By 15kg ammonium formate, 1kg methylamine catalyst, 10kg water, 5kg ethylene glycol are added in reactor, opened Dynamic stirring, control pressure is not higher than 0.5MPa, and below 120 DEG C reactor is added portionwise in 12kg oxirane by temperature control In, react 5 hours.Cool after the completion of reaction, then control vacuum below 600 millimetress of mercury, to depressurize below 100 DEG C of temperature The unnecessary water of removing, removes vacuum, cools to and product is released after less than 50 DEG C.Obtain compound C-1.Viscosity is about 200 centipoises, pH=8.5, decomposition temperature is higher than 100 DEG C.

Embodiment C-2

Embodiment C-1 is repeated, simply 12kg oxirane is replaced using 15kg expoxy propane, and expoxy propane is not It is to add in batches in reactor, but is disposably added thereto.Obtain compound C-2.Viscosity is about 350 centipoises, pH= 8.6, decomposition temperature is higher than 100 DEG C.

Embodiment C-3

By 10kg methyl formate, 10kg Ethyl formate, 13kg ammoniacal liquor (concentration 25wt%), 35kg diethanol amine It is added in reactor, starts stirring, control pressure is not higher than 0.5MPa, is slowly heated up in the case where being stirred continuously, when temperature rise Reacted 15 hours to temperature control at 100 DEG C.Cool after the completion of reaction, it is temperature below 600 millimetress of mercury then to control vacuum Less than 100 DEG C removed under reduced pressure methanol and ethanol, remove vacuum, cool to less than 50 DEG C and release after product.Obtain compound C-3. Viscosity is about 400 centipoises, and pH=9, decomposition temperature is higher than 100 DEG C.

Above-claimed cpd C-1, C-2 and C-3 release carbon dioxide immediately when being contacted with isocyanates, while also putting Go out a small amount of CO gas, overcome the shortcoming of general physical blowing agent such as methyl formate.

Implement row C-4 (being not belonging to logical formula (I) compound)

24kg ammoniacal liquor (concentration 25wt%) is added in reactor, control temperature is being stirred continuously below 100 DEG C It is lower to be slowly added drop-wise to 20kg formic acid (concentration 85wt%) in ammoniacal liquor, add rear insulation reaction 1 hour, then control vacuum Below 600 millimetress of mercury, the unnecessary water of removed under reduced pressure below 100 DEG C of temperature.Obtain compound C-4.Viscosity is about 150 Centipoise, pH=9.5, decomposition temperature is higher than 100 DEG C.

Embodiment C-5 (is not belonging to logical formula (I) compound)

23kg ammoniacal liquor (concentration 25wt%), 1.5kg dimethylamine are added in reactor, control temperature is at 100 DEG C Hereinafter, be stirred continuously it is lower 20kg formic acid (concentration 85wt%) is slowly added drop-wise in ammoniacal liquor, add rear insulation reaction 1 small When, vacuum is then controlled for below 600 millimetress of mercury, the unnecessary water of removed under reduced pressure, removes vacuum below 100 DEG C of temperature, Cool to after less than 50 DEG C and release product acquisition compound C-5.Viscosity is about 150 centipoises, and pH=9.2, decomposition temperature is higher than 100℃。

Embodiment C-6 (is not belonging to logical formula (I) compound)

23kg ammoniacal liquor (concentration 25wt%), 1.5kg methylamine are added in reactor, control temperature 100 DEG C with Under, be stirred continuously it is lower 20kg formic acid (concentration 85wt%) is slowly added drop-wise in ammoniacal liquor, add rear insulation reaction 1 hour, Then vacuum is controlled for below 600 millimetress of mercury, the unnecessary water of removed under reduced pressure below 100 DEG C of temperature (such as can reach 10wt% or so water content), remove vacuum, cool to and product is released after less than 50 DEG C.Compound C-6 is obtained, is not tied It is brilliant, it may be possible to which that the methylamine added disturbs its crystallization.Viscosity is about 150 centipoises, and pH=9, decomposition temperature is higher than 100 DEG C.

Compound C-4, C-5 or C-6 send carbon dioxide immediately when being contacted with isocyanates, while also releasing few CO gas is measured, the shortcoming of general physical blowing agent is overcome.

Although compound C-1 to C-6 is not decomposed even at higher than 110 DEG C, inventor has found by experiment, These can easily decompose and discharge CO during polyurethane foam₂, reason is probably to work as to touch isocyanates chemical combination React the carbonic anhydride for generating less stable during thing with NCO group first.

D)Prepare the logical formula (I) compound with bicarbonate radical (HO-COO-)

Embodiment D-1

10kg ammonium hydrogen carbonate (molecular weight 79.06), 9.0kg water and 1kg ethylenediamines are added to transparent quartzy glass In glass reactor, stirring and dissolving (allows the presence of undissolved ammonium hydrogen carbonate), seals reactor, then in the case where being stirred continuously, control Temperature processed is between 45-65 DEG C, and control pressure is not higher than 0.6MPa, and 20kg expoxy propane is added portionwise in reactor, Add rear temperature control to react 10 hours, then cool to 50 DEG C, control vacuum removes unnecessary water under below 600mHg decompressions, Cool to and vacuum is bled off after less than 40 DEG C, product is released.Obtain compound D-1.Viscosity is about 250 centipoises.PH=8, Decomposition temperature is at 36-42 DEG C.

Inventor it was unexpectedly observed that when compound D-1 be mixed with PPG and/or PEPA, for example with During composition, foam (" white material ") processed, the decomposition temperature for the compound D-1 being dissolved in white material can be improved to 45-65 DEG C.This So that compound D-1 has suitable decomposition temperature, therefore, be suitable for polyurethane foam.

E)Preparing has carbonic acid list hydrocarbyl carbonate (R^bO-COO^-) anion logical formula (I) compound

Embodiment E-1

Ammonium salt (molecular weight 93), 9.0kg water and the 1kg ethylenediamines of 10kg bicarbonate methyl esters are added to transparent stone In English glass reactor, stirring and dissolving (allows the presence of undissolved ammonium salt), seals reactor, then in the case where being stirred continuously, control Temperature processed is between 45-65 DEG C, and control pressure is not higher than 0.6MPa, and 20kg expoxy propane is added portionwise in reactor, Add rear temperature control to react 10 hours, then cool to 50 DEG C, control vacuum removes unnecessary water under below 600mHg decompressions, Cool to and vacuum is bled off after less than 40 DEG C, product is released.Obtain compound E-1.Viscosity is about 350 centipoises.PH=8, Decomposition temperature is at 42 DEG C -60 DEG C.

F)Preparing has-OOC-N (R¹)-R^a-N(R²)-COO- or R^a'(-N(R¹)-COO-)₃The logical formula (I) of anion Compound

Embodiment F-1

By 10kg NH₄OOC-NH-(CH₂)₅-NH-COO NH₄(molecular weight 182), 9.0kg water are added to transparent stone In English glass reactor, stirring and dissolving (allows the presence of undissolved ammonium salt), seals reactor, then in the case where being stirred continuously, control Temperature processed is between 45-55 DEG C, and control pressure is not higher than 0.6MPa, and 20kg expoxy propane is added portionwise in reactor, Add rear temperature control to react 10 hours, then cool to 50 DEG C, control vacuum removes unnecessary water under below 600mHg decompressions, Cool to and vacuum is bled off after less than 40 DEG C, product is released.Obtain compound F-1.Viscosity is about 600 centipoises.PH=9, Decomposition temperature is at 45 DEG C -70 DEG C.

Embodiment F-2

By the 12kg benzene -1,3,5- three (aminoquinoxaline) (molecular weight 306) with following formula：

It is added to 9.0kg water in transparent quartz glass reactor, stirring and dissolving (allows the presence of undissolved ammonium Salt), reactor is sealed, then in the case where being stirred continuously, control temperature is between 45-60 DEG C, and control pressure is not higher than 0.6MPa, will 20kg expoxy propane is added portionwise in reactor, is added rear temperature control and is reacted 10 hours, then cool to 50 DEG C, controls vacuum Unnecessary water is removed under below 600mHg decompressions, cools to and vacuum is bled off after less than 40 DEG C, product is released.Changed Compound F-2.Viscosity is about 510 centipoises.PH=9.6.Decomposition temperature is at 45 DEG C -70 DEG C.

G)Prepare the logical formula (I) compound with primitive nail acid radical anion

Embodiment G-1

15kg triethyl orthoformate, 20kg diethanol amine, 10kg water are added in reactor, stirring is started, Control pressure is not higher than 0.1MPa, is slowly heated up in the case where being stirred continuously, when when temperature is increased to 80 DEG C, temperature control reaction 10 is small.Instead 50 DEG C are cooled to after the completion of answering, it is the following removed under reduced pressure ethanol of temperature 50 C below 600 millimetress of mercury then to control vacuum, Cool to less than 40 DEG C release products after produce compound G-1, viscosity is about 500 centipoises, pH=8.0, and decomposition temperature is in 45- 70℃。

Embodiment G-2

15kg trimethyl orthoformate, 2.0kg ethylene glycol, 10kg water, 6.0kg ethylenediamine are added to reactor In, stirring is started, control pressure is not higher than 0.1MPa, is slowly heated up in the case where being stirred continuously, the temperature control when temperature is increased to 70 DEG C Reaction 5 hours.Cool after the completion of reaction, then control vacuum below 600 millimetress of mercury, piptonychia is depressurized below temperature 50 C Alcohol, removes vacuum, and compound G-2, about warm 250 centipoise of viscosity, pH=can be obtained after cooling to less than 40 DEG C releasing products 8.3,45-70 DEG C of decomposition temperature.

Embodiment G-3

15kg triethyl orthoformate, 13kg monoethanolamine, 7.0kg water are added in reactor, stirring is started, Slowly heated up in the case where being stirred continuously, temperature control reacts 8 hours below 100 DEG C.Cool after the completion of reaction, then control the vacuum to be Below 600 millimetress of mercury, the following removed under reduced pressure ethanol of temperature 50 C removes vacuum, cools to less than 50 DEG C and releases after product i.e. The compound G-3 of two ester group hydrolyses of wherein triethyl orthoformate is obtained.The centipoise of viscosity about 300, pH=8.1, 45-70 DEG C of decomposition temperature.

Embodiment G-4

The ammoniacal liquor of 20kg orthoformic acid glycol ester, 11kg diethanol amine, 10kg is added in reactor, starts and stirs Mix, slowly heated up in the case where being stirred continuously, temperature control, which is no more than at 100 DEG C, to react 8 hours.Cool after the completion of reaction, then control true Reciprocal of duty cycle is that the unnecessary water of the following removed under reduced pressure of temperature 50 C removes vacuum, cools to less than 40 DEG C below 600 millimetress of mercury Compound G-4 can be obtained after releasing product.The centipoise of viscosity about 500, pH=8,45-70 DEG C of decomposition temperature.

Application Example

Embodiment 1

It regard 8 parts by weight as the compound A-1 that is prepared by above example A-1 of foaming agent, the polyethers of 50 parts by weight Foam stabiliser DC3201 (the US Air gasifications of polyalcohol 4110 (being produced by the Bin Hua groups of Shandong Province Accessories during Binzhou), 1 parts by weight Work company produce), the fire retardant TCPP (Jiangsu Yoke Chemical Co., Ltd.'s production) and 2 part by weight of catalyst of 12.5 parts by weight Transparent composition, foam is obtained after A33 (33LV, the production of air chemical company of the U.S.) is well mixed, is then added wherein 95.5 parts of isocyanates MDI (PM200, Yantai Wanhua chemical groups limited company), agitated uniform rear foaming is made poly- Urethane foamed material.Rate of closed hole>95%.

Embodiment 2

It regard 8 parts by weight as the compound A-2 that is prepared by above example A-2 of foaming agent, the polyethers of 30 parts by weight The PEPA CF6320 (Jiangsu Fu Sheng new materials Co., Ltd) and the foam of 1 parts by weight of polyalcohol 4110,20 parts by weight Transparent foaming is obtained after stabilizer DC3201, the fire retardant TCPP of 12.5 parts by weight and 2 part by weight of catalyst A33 are well mixed Composition, then adds 95.5 parts of isocyanates MDI (PM200) wherein, and polyurethane foam is made in agitated uniform rear foaming. Rate of closed hole>97%.

Embodiment 3

The compound A-3's, the foam stabiliser DC3201 of 2 parts by weight, 0.5 parts by weight as foaming agent of 20 parts by weight The catalyst PC-5 (US Air gasification work) of catalyst dibutyltin dilaurylate, 0.5 parts by weight, the catalyst PC- of 1 parts by weight 8 (US Air gasification works), the catalyst PT304 (US Air gasification work) of 1 parts by weight, the catalyst A33 of 1 parts by weight, 40 weight The fire retardant TCPP, the PPG 4110 of 20 parts by weight, the AKS7004 (AEKYUNG of 10 parts by weight of part PETROCHEMICAL CO., LTD KOREA), MN500 (Shandong Lanxing Dongda Chemical Co., Ltd, hydroxyl of 10 parts by weight Value mgKOH/g：It is uniform mixed 330-350) with the PEPA CF6320 (Jiangsu Fu Sheng new materials Co., Ltd) of 10 parts by weight With 50kg consumptions after conjunction, through flush coater and isocyanates MDI (PM200) according to volume ratio 1:(i.e. " white material " is with MDI's by 1-1.6 Volume ratio) spraying prepares polyurethane foamed material.Rate of closed hole>97%.

Embodiment 4

It regard 7 parts by weight as the compound A-4 of foaming agent, the catalyst PC-41 (US Air gasification work) of 1 parts by weight, 0.5 The catalyst PC-8 (US Air gasification work) of parts by weight, the parts by weight of pentamethylene 13, the foam stabiliser DC8545 of 2 parts by weight are (beautiful State's air chemical industry) it is added to PPG 2010 (Jiangsu Hai'an Petrochemical Plant produces), 25 parts by weight of 50 parts by weight PPG SA380 (Shandong Inov Polyurethane Co., Ltd.) and 25 parts by weight PPG SA460 (mountains An eastern Nowe polyurethane limited company) mixture in be well mixed, obtain transparent composition, foam (referred to as " white Material "), the system that foamed in 148.2 parts of isocyanates MDI (PM200), agitated uniform rear injection foaming mould is then added wherein Obtain belt leather polyurethane foamed material.Rate of closed hole>98%.

Sample is taken, 100 times of observation abscesses are amplified using SEM after being cut into slices with blade.As shown in Figure 4, cell diameter is 205 Micron.

As a comparison, the present embodiment 4 is repeated, simply 5 parts by weight water and the pentamethylene (1 of 12 parts by weight:2.4 weight ratios) use Make foaming agent, obtain contrast foams 4-1；As shown in Figure 5, cell diameter is 396 microns.

In addition, repeating the present embodiment 4, simply the compounds of this invention A-4 and pentamethylene (1:1.5 weight ratios) it is used as foaming Agent, is obtained with reference to foams 4-2；As shown in Figure 6, cell diameter is 306 microns.As a comparison, the present embodiment 4 is repeated, only It is water+LBA+ pentamethylene (1:1:1 weight ratio) it is used as foaming agent, obtain contrast foams 4-3, as shown in Figure 7, cell diameter For 495 microns.The present embodiment 4 is repeated, simply the compounds of this invention A-4, LBA and pentamethylene (1:1.2:1.3 weight ratios) it is used as Foaming agent, obtains and refers to foams 4-4, as shown in Figure 8, cell diameter is 335 microns.

As can be seen that foams seem fine and smooth, uniform, fine and close from Fig. 4, Fig. 6 and Fig. 8, abscess quantity in unit area It is obvious many.As can be seen that the diameter of abscess is substantially uneven from Fig. 5, Fig. 7, abscess quantity is substantially on the low side in unit area.

Embodiment 5

Using 6 parts by weight, as the foam stabiliser DC3201 of the compound A-5 of foaming agent, 1 parts by weight, (US Air gasifies Work) PPGs 4110 (Binzhou City, Shandong Province Bin Hua groups) of 30 parts by weight, the PEPA CF6320 (rivers of 20 parts by weight Su Fusheng new materials Co., Ltd), 0.5 part by weight of catalyst PC-41 (US Air gasification work), be well mixed after obtain foaming group Compound, then adds 85 parts by weight isocyanates MDI (PM200) wherein, and polyurethane foam is made in agitated uniform rear foaming. Rate of closed hole>97%.

Embodiment 6

It regard 20 parts by weight as the compound A-6 of foaming agent, PPG 2010 (Jiangsu Province Hai'an of 50 parts by weight Petrochemical plant produce), the PPG SA380 (Shandong Inov Polyurethane Co., Ltd.'s production) of 25 parts by weight and PPG SA460 (Shandong Inov Polyurethane Co., Ltd.), the catalyst PC- of 0.5 parts by weight of 25 parts by weight 41 (US Air gasification works), the catalyst PC-8 (US Air gasification work) of 0.5 parts by weight obtain transparent foaming after being well mixed Composition, then adds 175 parts of isocyanates MDI (PM200) wherein, and polyurethane foam material is made in agitated uniform rear foaming Material.Rate of closed hole>97%.

Embodiment 7

Using the compound A-7 as foaming agent, the 10 parts by weight HFC-365mfc of 4 parts by weight, the polyethers of 11 parts by weight is more First alcohol 4110 (Shandong Binzhou Bin Hua groups), PEPA DM2003 (the limited public affairs of Guangdong dolantin fine chemistry industry of 39 parts by weight Department), the foam stabiliser DC3201 (US Air gasification work) of 1.5 parts by weight and the catalyst JXP-508 (US Airs of 1 parts by weight Gasify work), the catalyst JXP-509 (US Air gasification work) of 0.6 parts by weight, catalyst K-15 (U.S.'s air of 1.5 mass point Chemical industry) it is well mixed after obtain composition, foam, the fire retardant TCPP of 25 parts by weight and then add the different of 155 parts by weight wherein Polyurethane foam is made in cyanate MDI (PM200), agitated uniform rear foaming.Rate of closed hole 93%.

Embodiment 8

Using the compound A-1 as foaming agent, the 10 parts by weight HFC-365mfc of 4 parts by weight, the polyethers of 15 parts by weight is more First alcohol 4110 (Shandong Binzhou Bin Hua groups), PEPA DM2003 (the limited public affairs of Guangdong dolantin fine chemistry industry of 35 parts by weight Department), catalyst PC-8 (US Air gasification work), 0.5 weight of the foam stabiliser DC3201 of 1.5 parts by weight and 0.5 parts by weight Composition, foam, the fire retardant TCPP of 25 parts by weight are obtained after the catalyst PC-41 (US Air gasification work) of part is well mixed, so Add 160 parts of isocyanates MDI (PM200) wherein afterwards, it is agitated it is uniform after foaming polyurethane foamed material is made.Closed pore Rate 92%.

Embodiment 9

Using 7 parts by weight as the compound A-3 of foaming agent, the catalyst PC-41 (US Air gasification work) of 1 parts by weight, The catalyst PC-8 (US Air gasification work) of 0.5 parts by weight, the parts by weight of pentamethylene 13, the foam stabiliser DC8545 of 2 parts by weight (US Air gasification work) is added to the PPG 2010 (Jiangsu Hai'an Petrochemical Plant's production) of 50 parts by weight, 25 weight (the Nowe polyurethane share of Shandong one is limited by the PPG SA380 (Shandong) of part and the PPG SA460 of 25 parts by weight Company) mixture in be well mixed, then add 150 parts of isocyanates MDI (PM200) wherein, it is agitated it is uniform after send out It is brewed to obtain polyurethane foam.Rate of closed hole 93%.

Embodiment 10

Using the compound A-2,8 parts by weight HFC-365mfc, 30 parts by weight as foaming agent of 5 parts by weight polyether polyols Alcohol 4110 (Shandong Binzhou Bin Hua groups), the PEPA CF6320 (Jiangsu Fu Sheng new materials Co., Ltd) of 20 parts by weight and The foam stabiliser DC3201 (US Air gasification work) of 1 parts by weight, (refined gram of Jiangsu chemical industry has the fire retardant TCPP of 12.5 parts by weight Limit company) and 1 part by weight of catalyst A33 (33LV, US Air gasification work), catalyst PC-41 (the US Air gasifications of 1 parts by weight Work) it is well mixed after obtain composition, foam, 102 parts of isocyanates MDI (PM200) are then added wherein, it is agitated uniform Foam afterwards and polyurethane foam is made.Rate of closed hole 92%.

Table 1：The performance of polyurethane foam

Wherein shrinkage factor (size changing rate) is measured according to chinese national standard GB/T 8811-2008, simply standing time For 5 months.Similarly hereinafter.

The product of wherein embodiment 4 seems fine and smooth, uniform, fine and close, as shown in figure 4, with good heat-insulating property, can Meet the requirement of the various performances in refrigerator and refrigerator-freezer field.The product of embodiment 5 disclosure satisfy that various in polyurethane pipe insulation The requirement of performance.The product of embodiment 6 seems very fine and smooth, uniform, densification, disclosure satisfy that LNG (liquefied natural gas) conveying guarantors The requirement of the cold various performances of application.The product of embodiment 7 disclosure satisfy that the requirement of the various performances of polyurethane heated board.Embodiment 8 product disclosure satisfy that polyurethane colorful steel plate, the requirement of the various performances of cold storage plate.

Embodiment 11

It regard 7 parts by weight as the compound B-1 that is prepared by above example B-1 of foaming agent, the polyethers of 50 parts by weight Foam stabiliser DC3201 (US Air gasification work), 12.5 weights of polyalcohol 4110 (Binzhou City, Shandong Province Bin Hua groups), 1 parts by weight The fire retardant TCPP (Jiangsu Yoke Chemical Co., Ltd.) and 2 part by weight of catalyst A33 (33LV, US Air gasification work) for measuring part are mixed Transparent composition, foam is obtained after conjunction is uniform, 95.5 parts of isocyanates MDI (PM200) are then added wherein, it is agitated equal Polyurethane foamed material is made in foaming after even.Rate of closed hole>97%.

Embodiment 12-20

Embodiment 12-20 repeats embodiment 2-10 respectively, and simply foaming agent is as shown in table 2.Embodiment 12-16 foam The rate of closed hole of body is all>98%.

Table 2：The performance of polyurethane foam

The product of wherein embodiment 14 has good heat-insulating property, disclosure satisfy that the various performances in refrigerator and refrigerator-freezer field Requirement.The product of embodiment 15 disclosure satisfy that the requirement of various performances in polyurethane pipe insulation.The foam production of embodiment 16 Product seem finer and smoother, uniform, densification, as shown in figure 9, therefore, it disclosure satisfy that LNG (liquefied natural gas) conveys cold insulation application The requirement of various performances.The product of embodiment 17 disclosure satisfy that the requirement of the various performances of polyurethane heated board.Embodiment 18 Product disclosure satisfy that polyurethane colorful steel plate, the requirement of the various performances of cold storage plate.

Embodiment 21

It regard 4 parts by weight as the compound C-1 that is prepared by above example C-1 of foaming agent, the polyethers of 50 parts by weight Polyalcohol 4110, the foam stabiliser DC3201 of 1 parts by weight, (refined gram of Jiangsu chemical industry is limited by the fire retardant TCPP of 12.5 parts by weight Company) and 1 part by weight of catalyst A33 (33LV, US Air gasification work), the catalyst PC-41 (US Air gasification work) of 1 parts by weight Transparent composition, foam is obtained after well mixed, 104.5 parts of isocyanates MDI (PM200) are then added wherein, it is agitated Polyurethane foam is made in foaming after uniform.Rate of closed hole>98%.

Embodiment 22

It regard 4 parts by weight as the compound C-2 that is prepared by above example C-2 of foaming agent, the polyethers of 30 parts by weight Polyalcohol 4110, the PEPA CF6320 (Jiangsu Fu Sheng new materials Co., Ltd) of 20 parts by weight, the resistance of 12.5 parts by weight Fire agent TCPP (Jiangsu Yoke Chemical Co., Ltd.), foam stabiliser DC3201 (US Air gasification work), 0.5 weight of 1 parts by weight Measure and obtain saturating after part catalyst PC-8 (US Air gasification work), 1 part by weight of catalyst PC-41 (US Air gasification work) are well mixed Bright composition, foam, then adds part isocyanates MDI (PM200) wherein, and polyurethane is made in agitated uniform rear foaming Foam.Rate of closed hole>97%.

Embodiment 23

By the compound C-3 prepared by above example C-3 of 3.5 parts by weight, the foam stabiliser DC3201 of 2 parts by weight (US Air gasifies by (US Air gasification work), 1 part by weight of catalyst PC-8 (US Air gasification work), 1 part by weight of catalyst PC-41 Work), 13 parts by weight pentamethylene, PPG 2010 (Jiangsu Hai'an Petrochemical Plant), 25 weights for being added to 50 parts by weight Measure the PPG SA380 (Shandong Inov Polyurethane Co., Ltd.'s production) of part and the PPG of 25 parts by weight Obtained after being well mixed in SA460 (production of Shandong Inov Polyurethane Co., Ltd. of manufacturer) mixture Transparent composition, foam is obtained, 145 parts of isocyanates MDI (PM200) are then added wherein, agitated uniform rear injection is foamed Foamed in mould and belt leather polyurethane foam is made.Rate of closed hole>98%.

Embodiment 24-26

Embodiment 24-26 repeats embodiment 21-23 respectively, and simply foaming agent is as shown in table 2.Rate of closed hole is equal>97%.

Table 3：The performance of polyurethane foam

Embodiment 27

Using 17 parts by weight as the compound D-1 that is prepared by above example D-1 of foaming agent, 100 parts by weight it is poly- Ethoxylated polyhydric alcohol 4110 (Shandong Binzhou Bin Hua groups), the foam stabiliser DC3201 (US Air gasification work) of 2 parts by weight and 2 weight Part catalyst A33 (33LV), the catalyst PC-41 (US Air gasification work) of 2 parts by weight obtain transparent foaming after being well mixed Composition, then adds 160 parts of isocyanates MDI (PM200) wherein, and polyurethane foam is made in agitated uniform rear foaming. Rate of closed hole>97%.

Embodiment 28

By the PPG 2010 of the compound E-1 of 25 parts by weight, 50 parts by weight, (Jiangsu Hai'an Petrochemical Plant gives birth to Production), the PPG SA380 (Shandong Inov Polyurethane Co., Ltd.'s production) of 25 parts by weight and 25 parts by weight gather Ethoxylated polyhydric alcohol SA460 (Shandong Inov Polyurethane Co., Ltd.), 2 parts by weight foam stabiliser DC3201 (US Airs Gasify work), 0.5 part by weight of catalyst PC-8 (US Air gasification work), 1 part by weight of catalyst PC-41 (US Air gasification work) mix The transparent composition, foam of uniform rear acquisition is closed, 155 parts of isocyanates MDI (PM200) are then added wherein, it is agitated uniform Foam afterwards and polyurethane foam is made.Rate of closed hole>97%.

Embodiment 29

By the compound F-1 of 15 parts by weight, 10 parts by weight pentamethylene, 2 parts by weight foam stabiliser DC3201 (US Airs Gasify work), 1 part by weight of catalyst PC-8 (US Air gasification work), 1.5 part by weight of catalyst PC-41 (US Air gasification work) plus Enter PPG 2010 (Jiangsu Hai'an Petrochemical Plant), the PPG SA380 of 25 parts by weight to 50 parts by weight (Shandong Inov Polyurethane Co., Ltd.'s production) and PPG SA460 (the manufacturer Shandong one of 25 parts by weight Nowe polyurethane limited company produce) in be well mixed after obtain transparent composition, foam, 150 are then added wherein Foam obtained belt leather polyurethane foam in part isocyanates MDI (PM200), agitated uniform rear injection foaming mould.Rate of closed hole> 97%.

Comparative example 1

Embodiment 28 is repeated, simply foaming agent is used as only with the pentamethylene of 15 parts by weight.Rate of closed hole 93%.

Table 4：The performance of polyurethane foam

Embodiment 30

It regard 12 parts by weight as the compound G-1 that is prepared by above example G-1 of foaming agent, the polyethers of 50 parts by weight Polyalcohol 4110, the foam stabiliser DC3201 of 1 parts by weight, (refined gram of Jiangsu chemical industry is limited by the fire retardant TCPP of 12.5 parts by weight Company) and 1 part by weight of catalyst A33 (33LV, US Air gasification work), the catalyst PC-41 (US Air gasification work) of 1 parts by weight Obtain composition, foam after well mixed, then add 104.5 parts of isocyanates MDI (PM200) wherein, it is agitated it is uniform after Polyurethane foam is made in foaming.Rate of closed hole>97%.

Embodiment 31

Using 7.5 parts by weight as the compound G-2 that is prepared by above example G-2 of foaming agent, 30 parts by weight it is poly- Ethoxylated polyhydric alcohol 4110, the PEPA CF6320 (Jiangsu Fu Sheng new materials Co., Ltd) of 20 parts by weight, 12.5 parts by weight Fire retardant TCPP (Jiangsu Yoke Chemical Co., Ltd.), the foam stabiliser DC3201 (US Air gasification work) of 1 parts by weight, 0.5 Obtained after part by weight of catalyst PC-8 (US Air gasification work), 1 part by weight of catalyst PC-41 (US Air gasification work) are well mixed Composition, foam, then adds part isocyanates MDI (PM200) wherein, and polyurethane foam is made in agitated uniform rear foaming. Rate of closed hole>97%.

Embodiment 32

By the compound G-3 prepared by above example G-3 of 9 parts by weight, the foam stabiliser DC3201 of 2 parts by weight (US Air gasifies by (US Air gasification work), 1 part by weight of catalyst PC-8 (US Air gasification work), 1 part by weight of catalyst PC-41 Work), 13 parts by weight pentamethylene, PPG 2010 (Jiangsu Hai'an Petrochemical Plant), 25 weights for being added to 50 parts by weight Measure the PPG SA380 (Shandong Inov Polyurethane Co., Ltd.'s production) of part and the PPG of 25 parts by weight Obtained after being well mixed in SA460 (production of Shandong Inov Polyurethane Co., Ltd. of manufacturer) mixture Composition, foam is obtained, is then added wherein in 145 parts of isocyanates MDI (PM200), agitated uniform rear injection foaming mould Belt leather polyurethane foam is made in foaming.Rate of closed hole>97%.

Embodiment 33

By the compound G-4 prepared by above example G-4 of 9.5 parts by weight, the foam stabiliser DC3201 of 2 parts by weight (US Air gasifies by (US Air gasification work), 1 part by weight of catalyst PC-8 (US Air gasification work), 1 part by weight of catalyst PC-41 Work), 13 parts by weight pentamethylene, PPG 2010 (Jiangsu Hai'an Petrochemical Plant), 25 weights for being added to 50 parts by weight Measure the PPG SA380 (Shandong Inov Polyurethane Co., Ltd.'s production) of part and the PPG of 25 parts by weight Obtained after being well mixed in SA460 (production of Shandong Inov Polyurethane Co., Ltd. of manufacturer) mixture Composition, foam is obtained, is then added wherein in 145 parts of isocyanates MDI (PM200), agitated uniform rear injection foaming mould Belt leather polyurethane foam is made in foaming.Rate of closed hole>97%.

Table 5：The performance of polyurethane foam

The performance of the CBA (abbreviation CFA) of the present invention

1st, the bin stability of composition, foam (referred to as white material) and foam performance test

1. .CFA-CP (abbreviation of pentamethylene) is used in mixed way the stability test for preparing and expecting in vain

We are according to the white material of the parameter configuration CFA-CP mixed systems of white material for refrigerator (in above example 9 White material), expect to determine white material activity after placing in 50 DEG C of baking ovens in vain, the reactivity expected in vain be measured by sampling every several days, it is real Test result such as table 5 below：

Table 5：The reactivity expected in vain

CT refers to rise time in table；GT refers to the wire drawing time.

As seen from the above table, the reactivity that changes of the CFA-CP in above-mentioned white material system over time is expected in vain is substantially not Become, it is generally acknowledged that can place more than half a year at normal temperatures after being placed 51 days at 50 DEG C.

In addition to reactivity, the foamed material thermal conductivity value prepared after CFA-CP mixing is also stabilization, the following is Foamed material (condition in the same manner as in Example 9) is prepared into after being sampled according to different time interval and to foamed material thermal conductivity factor It is tested etc. index, it is as a result as follows：

Date	Density kg/m³	Thermal conductivity factor (10 DEG C) λ w/mk
			2015.8.28	35	0.01917
2015.9.12	35	0.01923
			2015.9.24	35	0.01906
2015.10.15	35	0.01911

It can be seen from the table, although same white material standing time is different, the density of foaming does not change, and illustrates foaming effect Rate is constant, and thermal conductivity factor does not also change substantially.

2. CFA is only used only as the stability experiment of the white material prepared by foaming agent in

In the same manner as in Example 5, we are configured with the white material prepared completely using CFA in room temperature according to conventional white material formula It is lower to place 3 months, white material activity and the thermal conductivity factor of foam are measured by sampling every other month, measurement result is as follows：

Date	Reaction time	Thermal conductivity factor (10 DEG C) λ w/mk
			2013.11.27	CT:9 GT:25 TFT:32	0.02085
2014.1.24	CT:9 GT:24 TFT:32	0.02123
			2014.2.26	CT:9 GT:24 TFT:35	0.02093
2014.3.27	CT:9 GT:25 TFT:36	0.02140

TFT refers to the skinning unsticking time in table.

As can be seen from the above table, reacting condition activity and heat conduction of the CFA of the present invention more than in white material system over time Coefficient keeps stable.

3. CFA is freely steeped under low-density and the stability of Water blown is contrasted

Above example 5 is repeated, but the consumption of foaming agent changes into the compound A-4 of 15 parts by weight, meanwhile, as right Than repeating above example 5, but only with water as foaming agent, respective white material and respective foam material are prepared respectively Material, in the case of the density identical of the foamed material obtained observe two kinds of foamed materials change with time stability whether Change.Preparation time is on April 16th, 2015, and density is all 22kg/m³, Figure 10 and Figure 12 are the initial outer of foams of the present invention See, Figure 11 and Figure 13 are the initial appearance for using water as the foams prepared by foaming agent.It is placed into September in 2015 29, Five totally months, the outward appearance of foam is observed, Figure 14 is product of the present invention, and outward appearance and size have almost no change, and Figure 15 is contrast Expert thinks in sample atrophy, polyurethane row, when foam density is in 25kg/m³Contract bubble during left and right in the case of Water blown Problem is inevitable, and this is the maximum difference of CFA and water.In other words, Water blown is used for the fields such as external wall spraying Change foamed material over time is shunk, thermal conductivity factor degenerates.

Other application

1st, the application of foaming agent of the invention in the preparation of polystyrol foam material

Embodiment 34

By the polystyrene resin powder of 100 parts by weight, the foaming agent B-1 of the present invention of 6 parts by weight, particle mean size 175 is micro- The calcium carbonate of rice, the zinc stearate of 0.3 parts by weight, toner (the big prosperous board, Wei Chang pigment Co., Ltd of Shenzhen of 0.3 parts by weight Production) input mixer mixed at a temperature of 30-40 DEG C of scope, acquisition foamed polystyrene composition, then utilize (draw ratio of screw rod is 28 for single screw extrusion machine:1) extrusion molding, each section of temperature of extruder be：One section 85 DEG C~95 DEG C, two 95 DEG C~105 DEG C, three sections, 105 DEG C~115 DEG C, four sections 115 DEG C~125 DEG C of section；125 DEG C~130 DEG C of mold temperature；Screw rod turns Speed is 5rpm~9rpm.The apparent density of the section bar obtained is 587kg/m³.SEM photograph is as shown in figure 16 (100 times of amplification). From photo as can be seen that the diameter of abscess is than more uniform.

2nd, the application of foaming agent of the invention in the preparation of polyvinyl-chloride foam material

Embodiment 35

By the polyvinyl chloride resin of 85 parts by weight, the foaming agent A-1 of the present invention of 5 parts by weight, the Tissuemat E of 0.5 parts by weight is average The calcium carbonate that 175 microns of granularity, the zinc stearate of 0.3 parts by weight, toner (the big prosperous board, the big prosperous pigment in Shenzhen of 0.3 parts by weight Co., Ltd produce) input mixer mixed at a temperature of 30-40 DEG C of scope, acquisition foam polyvinyl chloride composition, Then using single screw extrusion machine, (draw ratio of screw rod is 28:1) extrusion molding, each section of temperature of extruder be：One section 145 DEG C ~150 DEG C, two sections 155 DEG C~165 DEG C, three sections, 175 DEG C~185 DEG C, four sections 180 DEG C~195 DEG C；195 DEG C of mold temperature~ 205℃；Screw speed is 5rpm~9rpm.The proportion of the section bar obtained is 0.55g/cm³。

Claims

1. the orthoformic acid organic amine salt compound with below general formula (I)：

A^n-[B^m+]_p (I)

In formula, A^n-It is primitive nail acid group：(g)

In formula, R ' is H, the C optionally replaced by hydroxyl or amino or halogen₁-C₂₆Alkyl (preferably C₁-C₁₀Alkyl, more preferably C₁-C₃ Alkyl), or C₁-C₂₆Acyl group (preferably C₁-C₁₀Acyl group, more preferably C₁-C₇Acyl group)；

Bm+ be or comprising：The ammonium ion of+1 valency and/or with m-⁺NR³R⁴H groups and/or-⁺NR³One kind of H- groups or A variety of organic amine B cation；

Wherein m=1-10, preferably m=1-5；

Wherein, R³Or R⁴Independently selected from：H, R, the C optionally replaced by hydroxyl or amino or halogen₁-C₇Aliphatic alkyl is (preferably C₁-C₄Alkyl), the C optionally replaced by hydroxyl or amino or halogen₃-C₇Cyclic aliphatic alkyl (such as cyclobutyl or cyclohexyl), Huo,Ren Select the C replaced by hydroxyl or amino or halogen₆-C₁₀Aromatic hydrocarbyl (preferably phenyl or aminomethyl phenyl)；

Precondition is：The R in the compound of above-mentioned logical formula (I)³Or R⁴In at least one be the R group being connected with N atoms, or The compound of the logical formula (I) has at least one R group bonded with N；

Wherein one or more of the R group in following groups：

(1a)H[OCH(R_1a)CH(R_2a)]_q-, such as H (OCH₂CH₂)_q-、H(OCH₂CH(CH₃))_q-、H(OCH(CH₃)CH₂)_q-、H (OCH₂CH(C₆H₅))_q-、H(OCH(C₆H₅)CH₂)_q-、H(OCH₂CH(CH₂Cl))_q-、H(OCH(CH₂Cl)CH₂)_q- or H (OCH₂CH (CBr₃))_q-；

(2a)H[OCH(R_1a)CH(R_2a)CH(R_3a)]_q-；Or

(3a)H[OCH(R_1a)CH(R_2a)CH(R_3a)CH(R_4a)]_q-；

Wherein q value or average value are q=1-50；R_1a、R_2a、R_3aOr R_4aIt is each independently selected from：H, optionally by hydroxyl or amino Or the C of halogen substitution₁-C₇Aliphatic alkyl, the C optionally replaced by hydroxyl or amino or halogen₃-C₇Cyclic aliphatic alkyl, Huo,Ren Select the C replaced by hydroxyl or amino or halogen₆-C₁₀Aromatic hydrocarbyl.

2. the compound according to required by claim 1, wherein q=1-20, more preferably 1-5, more preferably q=1-4, more preferably q =1-3, particularly preferred q=1-2.5, particularly preferred q=1.5-2.0, by q mean value calculation, or q is 5-50, more preferably 10-20。

3. the compound according to required by claim 1 or 2, wherein organic amine B have m to m+3 primary amine, secondary amine and/or Tertiary amine group, and optionally there is quaternary ammonium group.

4. the compound according to any one of claim 1-3, wherein B^m+Two or more above-mentioned organic amines sun from The combination of son or mixture.

5. the compound according to any one of claim 1-4, wherein R³Or R⁴Independently selected from：H, R, optionally by hydroxyl Base or the C of amino or halogen substitution₁-C₄Aliphatic alkyl, the cyclobutyl optionally replaced by hydroxyl or amino or halogen or hexamethylene Base, or, the phenyl or aminomethyl phenyl optionally replaced by hydroxyl or amino or halogen；It is further preferred that R_1a、R_2a、R_3aOr R_4aIt is each independent Ground is selected from：H, methyl or the ethyl optionally replaced by hydroxyl or amino or halogen, or optionally taken by hydroxyl or amino or halogen The propyl group or isopropyl in generation, the cyclohexyl optionally replaced by hydroxyl or amino or halogen, or, optionally by hydroxyl or amino or halogen Substituted phenyl or aminomethyl phenyl.

6. compound according to claim 5, wherein R_1a、R_2a、R_3aOr R_4aIt is each independently selected from：H, methyl, chloromethane Base, bromomethyl, ethyl, cyclohexyl, or, phenyl.

7. the compound according to any one of claim 1-6, its pH is 7.5-10, preferably 7.8-9.5, more excellent Select pH 8-9；And/or the content of its alkali and alkaline earth metal ions be 0-200ppm (quality), more preferably less than 100ppm, more Preferably shorter than 10ppm, most preferably below detectable limit or for 0ppm.

8. the compound according to any one of claim 1-7, the content of its water is 0-40wt%, preferably 5- 35wt%, more preferably 10-30wt%, more preferably 15-25wt%；And/or, the compound average per molecule of logical formula (I) contains 1.5-5 R group.

9. preparing the method for the compound of the logical formula (I) of any one in claim 1-8, this method includes：Orthoformic acid esters Compound in a solvent, optionally in the presence of a catalyst, and is belonging to the organic amine M of Organic Alcohol amine or with least one Reaction is hydrolyzed in the presence of the compound B and water that belong to Organic Alcohol amine of individual above-mentioned N-R groups；Wherein, the water Amount is sufficient so that at least two ester group hydrolyses of orthoformic acid ester type compound, it is further preferred that the amount of water is enough to make Obtain three ester group hydrolyses of orthoformic acid ester type compound；

Wherein organic amine compound B be organic amine compound (M) as initiation material or as initiator, with epoxides Reacted what is formed, one or more of the epoxides in these following epoxides：

Or styrene oxide,

Wherein described organic amine compound (M) is selected from following organic amine compound in these：

C₁-C₂₄Alkyl amine；

Two (C₁-C₁₆Alkyl) amine；

Optionally in C₂-C₁₄The C being optionally substituted by a hydroxyl group on alkylene₂-C₁₄Alkylene Diamines；

Optionally in C₂-C₁₄The C being optionally substituted by a hydroxyl group on alkylene₄-C₁₆Polyalkylenepolyamines class；

The C being optionally optionally substituted by a hydroxyl group with three primary amine groups₃-C₁₈Organic three amine is optional by hydroxyl with four primary amine groups The C of base substitution₅-C₁₈Organic tetraamine；Or

C₂-C₁₀Alcamines.

10. method according to claim 9, the wherein epoxides are：Oxirane, expoxy propane, epoxychloropropane, Epoxy bromopropane, epoxy butane or epoxy chlorobutane or styrene oxide, and any two or a variety of mixing in them Thing.

11. the compound prepared as the method described in claim 9 or 10.

12. a kind of foaming agent, it includes the organic amine salt with logical formula (I) according to any one of claim 1-8 Compound or organic amine salt compound mixture, or formula (I) is led to as having according to any one of claim 1-8 Organic amine salt compound or organic amine salt compound mixture are constituted.

13. a kind of foaming agent, it includes compound according to claim 11.

14. the foaming agent according to claim 12 or 13, it is used as polyurethane foams, foamed polystyrene agent or polychlorostyrene Ethene foaming agent.

15. organic amine salt compound or the organic amine salinization with logical formula (I) according to any one of claim 1-8 Polymer mixtures as polyurethane foams, foamed polystyrene agent or foam polyvinyl chloride agent purposes.

16. polyurethane foamed composite thing, it is included：

The 0.01-100 weight % orthoformic acid organic amine with logical formula (I) according to any one of claim 1-8 Salt compound or organic amine salt compound mixture, or compound according to claim 11；

0-50 weight % physical blowing agent；

0-5 weight % water, and

0.0-99.99 weight % polymer polyatomic alcohol；Wherein, the percentage by weight is based on the total of polyurethane foamed composite thing Weight.

17. polyurethane foamed composite thing according to claim 16, it is included：

0.1-80 weight % (more preferably 1-70wt%, more preferably 3-60wt%, more preferably 5-50wt%, more preferably 7-40wt%, Such as 10wt%, 15wt%) the orthoformic acid organic amine salt with logical formula (I) according to any one of claim 1-8 Compound or organic amine salt compound mixture, or compound according to claim 11；

0-40 weight % physical blowing agent；

0-4 weight % water, and

20.0-99.9 weight % (more preferably 30-99wt%, more preferably 40-97wt%, more preferably 50-95wt%, more preferably 60- 93wt%, such as 90wt% or 85wt%) polymer polyatomic alcohol；Wherein, the percentage by weight is based on polyurethane foamed composite The gross weight of thing.

18. the polyurethane foamed composite thing according to claim 16 or 17, it contains the water of 0.5-4wt% altogether, more excellent Select 0.8-2.5wt%, more preferably 1-2.2wt% water.

19. the polyurethane foamed composite thing according to any one of claim 16-18, it is also included：Foam stabiliser, Catalysts for polyurethanes and fire retardant.

20. the polyurethane foamed composite thing according to any one of claim 16-19, wherein polymer polyatomic alcohol are selected From：It is PPG, PEPA, polyether-polyester polyol, PCDL, polycarbonate-polyester polyalcohol, poly- Carbonic ester-PPG, polybutadiene polyol or polysiloxane polyhydric alcohol.

21. the polyurethane foamed composite thing according to any one of claim 16-20, wherein composition, foam are transparent Or clarification.

22. the polyurethane foamed composite thing according to any one of claim 16-21, it has following characteristics：1) wrap Containing alcohol amine salt or alcohol amine compound；2) transparent or clarification；3) discharge in case of heating or in the case where adding acid CO₂；4) when composition, foam is contacted or mixed with isocyanates or polyisocyanates, the material being mixed to form was at 0.2-4 seconds Become milky in (preferably 1-2 seconds).

23. polyurethane foamed composite thing according to claim 21, wherein the material being mixed to form becomes milky, is accompanied by Volume rapid expanding phenomenon, but this process and it is non-foam it is real rise, material just starts to rise afterwards.

24. polyurethane foamed material, it passes through the polyurethane foamed composite thing and polyisocyanates any one of 16-22 Monomer or isocyanate-terminated prepolymer react and formed after being mixed.

25. polyurethane foamed material according to claim 24, wherein the polyurethane foamed composite thing and polyisocyanic acid The amount ratio (wt) of ester monomer or isocyanate-terminated prepolymer is 0.5:1-2:In the range of 1, preferably 0.5:1-1:1 In the range of.

26. the polyurethane foamed material according to claim 24 or 25, wherein in 34-42Kg/m³Density foam under, Thermal conductivity factor w/mk (10 DEG C) or w/mk (22.5 DEG C) are between 0.01900-0.02200, preferably in 0.01910- Between 0.02150.

27. the polyurethane foamed material according to any one of claim 24-26, its size changing rate or shrinkage factor ≤ 4.5%, preferably≤1.5%, more preferably≤0.5%；Especially after placing 5 months.