阅读说明：本技术 制备硬质聚氨酯泡沫的方法 (Process for preparing rigid polyurethane foams ) 是由 魏文平 李立强 高建伍 于 2020-06-05 设计创作，主要内容包括：本发明涉及一种用非连续生产工艺制备硬质聚氨酯泡沫的方法,以及该方法所制得的硬质聚氨酯泡沫及其用途。(The invention relates to a method for preparing rigid polyurethane foam by a discontinuous production process, rigid polyurethane foam prepared by the method and application of the rigid polyurethane foam.)

1. A method for preparing rigid polyurethane foam by a discontinuous production process, comprising:

injecting a polyurethane reaction system comprising the following components into a mold to prepare the rigid polyurethane foam:

component A, comprising: a polyisocyanate;

component B, comprising: polyether polyols having a functionality of from 2.0 to 8.0 and a hydroxyl number of from 50 to 550mgKOH/g, preferably from 90 to 450mgKOH/g (test method ISO 14900-2017);

wherein the angle of the mould relative to the horizontal plane when the polyurethane reaction system is foamed is more than or equal to 5 degrees, preferably more than or equal to 7 degrees, more preferably more than or equal to 10 degrees, and particularly preferably more than or equal to 30 degrees; and

the mold has at least one gate positioned below 1/2, preferably below 1/3, and more preferably below 1/4 near the horizontal plane in the height direction of the mold.

2. The method of claim 1, wherein the component B further comprises at least one of:

B1) polyether polyol having a functionality of not less than 4 and a hydroxyl value of < 400mgKOH/g (test method ISO 14900-2017), in an amount of from 5 to 45pbw, preferably from 7 to 25pbw, based on 100pbw of component B;

B2) polyether polyols having a functionality of > 4 and a hydroxyl number of > 400mgKOH/g (test method ISO 14900-2017) in an amount of from 20 to 70pbw, preferably from 30 to 65pbw, based on 100pbw of component B;

B3) an aromatic amine-initiated polyether polyol having a functionality of from 3.5 to 4.2, a hydroxyl number of < 400mgKOH/g (test method ISO 14900-2017) and a viscosity at 25 ℃ of < 30000 mPa.s (test method ISO 3219-1993), in an amount of from 5 to 35pbw, preferably from 10 to 20pbw, based on 100pbw of component B; and

B4) polyether polyols having a functionality of < 3 and a hydroxyl number of < 400mgKOH/g (test method ISO 14900-2017) in an amount of from 0 to 15pbw, preferably from 3 to 10pbw, based on 100pbw of component B.

3. The method of claim 1 or 2, wherein said component B further comprises:

B5) at least one flame retardant in an amount of 5 to 30pbw, preferably 10 to 20pbw, based on 100pbw of component B.

4. A process according to claim 3, characterized in that the non-halogen flame retardant is present in the flame retardant in an amount of 5 to 40% by weight, preferably 10 to 30% by weight, based on 100% by weight of the total weight of the flame retardant.

5. The method of claim 1 or 2, wherein the polyurethane reaction system further comprises: component C, at least one blowing agent, in an amount of 2 to 30 wt.%, preferably 5 to 25 wt.%, based on the total weight of component B of 100 wt.%.

6. Process according to claim 5, characterized in that the amount of water in the blowing agent is 0.5 to 4.0% by weight, preferably 1.0 to 2.5% by weight, based on the total weight of component B taken as 100% by weight.

7. The process as claimed in claim 1 or 2, wherein the thermal conductivity of the rigid polyurethane foam produced when the mould is at an angle of > 5 degrees, preferably > 7 degrees, more preferably > 10 degrees to the horizontal at 25 ℃ is reduced by > 1%, preferably > 2%, more preferably > 3%, particularly preferably > 5% compared to 0 degrees when the mould is at an angle to the horizontal when the polyurethane reaction system is foamed (test method ASTM C177-2010).

8. A rigid polyurethane foam obtained by the process for producing a rigid polyurethane foam according to any one of claims 1 to 7.

9. Rigid polyurethane foam according to claim 8, characterized in that the core density of the rigid polyurethane foam is from 30 to 80kg/m3, preferably from 35 to 65kg/m3 (test method ISO 845-.

10. Rigid polyurethane foam according to claim 8 or 9, characterized in that the rigid polyurethane foam has a thermal conductivity at 25 ℃ of 23.80 mW/mK or less, preferably 23.70 mW/mK or less, more preferably 23.60 mW/mK or less (test method ASTM C177-2010).

11. A polyurethane composite panel comprising a rigid polyurethane foam according to any one of claims 8 to 10.

12. A method of making the polyurethane composite panel of claim 11 comprising the steps of:

fixing the two surface layers; and

and injecting a polyurethane reaction system between the two surface layers, and carrying out reaction foaming molding on the polyurethane reaction system to obtain the polyurethane composite board.

13. The method of claim 12, wherein the two facings are secured by a mold comprising an upper cover and a lower cover, the two facings being secured to an inner surface of the upper cover and an inner surface of the lower cover, respectively.

14. An insulating device comprising a rigid polyurethane foam as claimed in any one of claims 8 to 10.

15. The insulating device of claim 14, wherein said insulating device is selected from the group consisting of a refrigerator, an ice chest, a freezer, a refrigerator car, a water heater, a holding tank, an incubator, and an insulated box.

Technical Field

The invention relates to a method for preparing rigid polyurethane foam by a discontinuous production process, rigid polyurethane foam prepared by the method and application of the rigid polyurethane foam.

Background

The polyurethane hard foam board has excellent performances of light weight and heat preservation, and can be widely applied to freezers, cold trucks, cold storages and buildings. In the production of polyurethane sandwich plates, the preparation of the non-continuous plates has the advantages of flexibility, simple process and the like, and plays an important role in the market.

In cold chain transportation, the thermal insulation performance of transportation equipment has been of great concern. How to improve the heat insulation performance of the product is also an important index pursued by various manufacturers.

The existing polyurethane composite material prepared by a discontinuous process is prepared by a discontinuous process, namely, a prefabricated shell is placed in a mould, polyurethane resin is injected into the mould, the mould is closed, the polyurethane resin foams to form polyurethane foam, and then the mould is removed, so that the polyurethane composite material is obtained. Polyurethane resins are generally made by mixing an isocyanate component and a polyol component. How to produce hard polyurethane foam with more excellent heat-insulating property on the premise of energy conservation, economy and environmental protection is a difficult problem to be solved urgently in the industry.

CN1239914A discloses a process for preparing soft foam products by injecting reaction raw materials with different density requirements in two times while keeping the mold angle at 40 °, but the influence of larger foaming angle on the system is not involved. Meanwhile, the preparation process of the soft foam is adopted, and the problems of heat preservation, air bubbles and the like of the foam are not involved.

CN102529008A proposes a process for preparing a large block of foam, which comprises raising the end of a mold close to a filling port to form a certain angle, cleaning and assembling the mold, forming a second preset angle between a filling pipe and the filling port, filling foam reaction raw materials, and finally forming the product. The process improves product quality, but the specific values for each angle and improvement in product quality are not mentioned. In addition, the process injection port is arranged at the highest position of the die.

Thus, despite the above disclosures, there is an urgent need in the industry for a process for making rigid polyurethane foams that more optimizes foam insulation properties.

Disclosure of Invention

In one aspect of the present invention, a method for preparing rigid polyurethane foam using a discontinuous production process is provided. The method comprises the following steps:

injecting a polyurethane reaction system comprising the following components into a mold to prepare the rigid polyurethane foam:

component A, polyisocyanate;

component B, comprising:

polyether polyols having a functionality of from 2.0 to 8.0 and a hydroxyl number of from 50 to 550mg KOH/g, preferably from 90 to 450mg KO H/g (test method ISO 14900-2017);

wherein the angle of the mould relative to the horizontal plane when the polyurethane reaction system is foamed is more than or equal to 5 degrees, preferably more than or equal to 7 degrees, more preferably more than or equal to 10 degrees, particularly preferably more than or equal to 30 degrees, and more particularly preferably more than or equal to 45 degrees; and

the mold is provided with at least one pouring gate, and the pouring gate is positioned below 1/2, preferably below 1/3, and more preferably below 1/4 in the height direction of the mold.

Preferably, the component B further comprises at least one of the following components:

B1) polyether polyol having a functionality of not less than 4 and a hydroxyl number of < 400mg KOH/g (test method ISO 14900-2017), in an amount of from 5 to 45pbw, preferably from 7 to 25pbw, based on 100pbw of component B;

B2) polyether polyols having a functionality of > 4 and a hydroxyl number of > 400mg KOH/g (test method ISO 14900-2017) in an amount of from 20 to 70pbw, preferably from 30 to 65pbw, based on 100pbw of component B;

B3) an aromatic amine-initiated polyether polyol having a functionality of from 3.5 to 4.2, a hydroxyl number of < 400mgKOH/g (test method ISO 14900-2017) and a viscosity at 25 ℃ of < 30000 mPa.s (test method ISO 3219-1993), in an amount of from 5 to 35pbw, preferably from 10 to 20pbw, based on 100pbw of component B;

B4) polyether polyols having a functionality of < 3 and a hydroxyl number of < 400mg KOH/g (test method ISO 14900-2017) in an amount of from 0 to 15pbw, preferably from 3 to 10pbw, based on 100pbw of component B; and

B5) at least one flame retardant in an amount of 5 to 25pbw, preferably 10 to 20pbw, based on 100pbw of component B.

Preferably, the non-halogen flame retardant is present in the flame retardant in an amount of 5 to 40 wt%, preferably 10 to 30 wt%, based on 100 wt% of the total weight of the flame retardant.

Preferably, the polyurethane reaction system further comprises: component C, at least one blowing agent, in an amount of 2 to 30 wt.%, preferably 5 to 25 wt.%, based on the total weight of component B.

Preferably, the blowing agent is selected from the group consisting of water, monofluorodichloroethane, cyclopentane, pentafluorobutane, pentafluoropropane, 1-chloro-3, 3, 3-trifluoropropene, 1-chloro-2, 3, 3, 3-tetrafluoropropene, hexafluorobutene, or combinations thereof.

Preferably, the amount of water in the blowing agent is from 0.5 to 4.0% by weight, preferably from 1.0 to 2.5% by weight, based on the total weight of component B.

Preferably, the thermal conductivity of the rigid polyurethane foam produced when the mold is foamed at an angle of not less than 5 degrees, preferably not less than 7 degrees, more preferably not less than 10 degrees, particularly preferably not less than 30 degrees, more particularly preferably not less than 45 degrees relative to the horizontal plane is reduced by not less than 1%, preferably not less than 2%, more preferably not less than 3%, and particularly preferably not less than 5% at 25 ℃ compared to when the mold is foamed at an angle of 0 degrees relative to the horizontal plane (test method ASTM C177-2010).

Preferably, the polyurethane reaction system further comprises a foam stabilizer in an amount of 1 to 5pbw, preferably 1.5 to 3pbw, based on 100pbw of component B.

Preferably, the polyurethane reaction system further comprises a catalyst comprising at least one of a blowing catalyst, a gelling catalyst, and a trimerization catalyst.

Preferably, the foaming catalyst is selected from one or a mixture of pentamethyldiethylenetriamine, bis-dimethylaminoethylether, N, N, N '-tetramethylethylenediamine, N, N, N' -tetramethylbutanediamine and tetramethylhexanediamine in any proportion; the gel catalyst is selected from one or a mixture of two of dimethylcyclohexylamine and dimethylbenzylamine in any proportion; the trimerization catalyst is selected from one or more than one of methyl ammonium salt, ethyl ammonium salt, octyl quaternary ammonium salt or hexahydro triazine and organic metal alkali in any proportion.

Through repeated experiments, we have unexpectedly found that the method for preparing rigid polyurethane foam, which comprises the improved processes, such as the angle of a mold relative to the horizontal plane when the polyurethane reaction system is foamed (≥ 5 degrees, preferably ≥ 7 degrees, more preferably ≥ 10 degrees, particularly preferably ≥ 30 degrees, more particularly preferably ≥ 45 degrees), the specific position of a pouring gate (the pouring gate is positioned below 1/2, preferably below 1/3, more preferably below 1/4 in the height direction of the mold), and the polyurethane reaction system adapted to the improved processes, simply and efficiently improves the heat insulation performance of the rigid polyurethane foam, and other physical properties are well maintained.

If the angle is too low during foaming of the mold, injected polyurethane reaction system raw materials are gathered near the injection port, so that the predistribution of the foaming reaction raw materials in the mold is not facilitated, and the quality conditions such as poor density distribution of foam, bubbles or poor density distribution at the flowing tail end of the foam and the like are caused. Meanwhile, the flowing of the raw materials in the mold before the initiation can cause the reduction of the heat insulation performance of the foam. Therefore, in the method for preparing rigid polyurethane foam of the present invention, when the pouring gate is set below 1/2, preferably below 1/3, and more preferably below 1/4 of the height of the mold, the pre-distribution of the reaction raw materials in the mold can be well improved, and the thermal insulation performance of the foam can be improved, thereby improving the performance of the whole polyurethane product.

In the prior discontinuous process, a material injection port is usually arranged at the highest position of a mould, and A and B (containing premixed physical foaming agents) are mixed by a foaming gun head and then injected into a cavity of the mould. In this process, when the reaction material is injected into the cavity from the highest position of the mold, a portion of the reaction material is attached to the upper end of the mold and the majority of the reaction material is injected into the bottom of the mold. When the foam expands, the two parts of raw materials are combined, and the heat insulation performance of the foam is affected. If the injection port is changed from the top to the middle of the mold, the amount of the raw material adhering to the mold during injection is reduced. When the material injection position is set to be the bottom of the mould, the reaction raw materials are injected to the bottom of the mould, and when the foam expands, the influence of multiple strands of reaction raw materials is avoided, so that the heat preservation and other physical properties of the foam can be ensured.

In another aspect of the present invention, there is provided a rigid polyurethane foam prepared by the method for preparing a rigid polyurethane foam of the present invention.

Preferably, the core density of the rigid polyurethane foam is 30-80kg/m3, preferably 35-65kg/m3 (test method ISO 845-2006).

Preferably, the rigid polyurethane foam has a thermal conductivity at 25 ℃ of 23.80 mW/mK or less, preferably 23.70 mW/mK or less, more preferably 23.60 mW/mK or less (test method ASTM C177-2010).

In yet another aspect of the present invention, there is provided a polyurethane composite panel comprising the rigid polyurethane foam of the present invention.

Preferably, the two face layer materials of the composite plate are selected from one or more of iron, aluminum, FRP, PS and ABS.

In still another aspect of the present invention, there is provided a method for preparing a polyurethane composite panel, comprising the steps of:

fixing the two surface layers; and

and injecting a polyurethane reaction system between the two surface layers, and carrying out reaction foaming molding on the polyurethane reaction system to obtain the polyurethane composite board.

Preferably, the two surface layers are fixed by a mold, the mold comprises an upper cover and a lower cover, and the two surface layers are respectively fixed on the inner surface of the upper cover and the inner surface of the lower cover.

In yet another aspect of the present invention, there is provided an insulation apparatus comprising the rigid polyurethane foam of the present invention.

Preferably, the insulation device is selected from the group consisting of a refrigerator, a freezer, a hot water heater, a hot tub, an incubator, and an insulated box.

Drawings

Fig. 1 shows a plan view of the mould in the method according to the invention at an angle of 30 degrees to the horizontal. Where 4 denotes a mold, 1 denotes a mold height, 2 denotes a gate, 3 denotes a mold angle, and 5 denotes a horizontal plane.

Fig. 2 shows a plan view of the mould in the method according to the invention at an angle of 60 degrees to the horizontal. Where 4 denotes a mold, 1 denotes a mold height, 2 denotes a gate, 3 denotes a mold angle, and 5 denotes a horizontal plane.

Fig. 3 shows a perspective view of the mould in the method according to the invention at an angle of 30 degrees to the horizontal. Where 4 denotes a mold, 1 denotes a mold height, 2 denotes a gate, and 3 denotes a mold angle.

Detailed Description

The following terms used in the present invention have the following definitions or explanations.

Bond strength, which is the strength at which the bonded portion is broken by applying a load/force;

thermal conductivity, which refers to the heat transferred by a material with unit thickness in a unit temperature difference and time and 1 square meter area under the condition of stable heat transfer, and the test method is ASTM C177-2010;

the core density refers to the foam center density tested under the condition of excessive filling in a mould used in the manufacturing process of the polyurethane composite board, namely the density of the molded foam core;

pbw refers to the mass parts of each component of the polyurethane reaction system;

functionality, means according to the industry formula: functionality ═ hydroxyl number^＊Molecular weight/56100; wherein the molecular weight is determined by GPC high performance liquid chromatography;

isocyanate index, which means a value calculated by the following formula:

the number of moles of isocyanate groups (NCO groups) in the A component

Components of polyurethane foam reaction system

A) Polyisocyanates

Any organic polyisocyanate may be used in the preparation of the rigid polyurethane foams of the present invention, including aromatic, aliphatic and cycloaliphatic polyisocyanates and combinations thereof. The polyisocyanate can be represented by the general formula R (NCO) n, wherein R represents an aliphatic hydrocarbon group having 2 to 18 carbon atoms, an aromatic hydrocarbon group having 6 to 15 carbon atoms, an araliphatic hydrocarbon group having 8 to 15 carbon atoms, and n is 2 to 4.

Useful polyisocyanates include, but are not limited to, vinyl diisocyanate, tetramethylene 1, 4-diisocyanate, Hexamethylene Diisocyanate (HDI), dodecyl 1, 2-diisocyanate, cyclobutane 1, 3-diisocyanate, cyclohexane 1, 4-diisocyanate, 1-isocyanato 3, 3, 5-trimethyl 5-isocyanatomethylcyclohexane, hexahydrotoluene 2, 4-diisocyanate, hexahydrophenyl 1, 3-diisocyanate, hexahydrophenyl 1, 4-diisocyanate, perhydrodiphenylmethane 2, 4-diisocyanate, perhydrodiphenylmethane 4, 4-diisocyanate, phenylene 1, 3-diisocyanate, phenylene 1, 4-diisocyanate, stilbene 1, 4-diisocyanate, mixtures thereof, and mixtures thereof, 3, 3-dimethyl-4, 4-diphenyldiisocyanate, toluene-2, 4-diisocyanate (TDI), toluene-2, 6-diisocyanate (TDI), diphenylmethane-2, 4 ' -diisocyanate (MDI), diphenylmethane-2, 2 ' -diisocyanate (MDI), diphenylmethane-4, 4 ' -diisocyanate (MDI), mixtures of diphenylmethane diisocyanates and/or homologues of diphenylmethane diisocyanates having more rings, polyphenylmethane polyisocyanates (polymeric MDI), naphthylene-1, 5-diisocyanates (NDI), their isomers, and any mixtures thereof.

Useful polyisocyanates also include isocyanates modified with a carbonized diamine, allophanate, or isocyanate, preferably, but not limited to, diphenylmethane diisocyanate, carbonized diamine-modified diphenylmethane diisocyanate, isomers thereof, mixtures thereof with isomers thereof.

When used in the present invention, the polyisocyanate includes an isocyanate dimer, trimer, tetramer or a combination thereof.

In a preferred embodiment of the invention, the polyisocyanate component is selected from polymeric MDI.

The organic polyisocyanates of the invention have an NCO content of 20 to 33 wt.%, preferably 25 to 32 wt.%, particularly preferably 30 to 32 wt.%. The NCO content was determined by GB/T12009.4-2016.

The organic polyisocyanates can also be used in the form of polyisocyanate prepolymers. These polyisocyanate prepolymers can be obtained by reacting an excess of the above organic polyisocyanate with a compound having at least two isocyanate-reactive groups at a temperature of, for example, 30 to 100 ℃, preferably about 80 ℃. The polyisocyanate prepolymers of the present invention have an NCO content of 20 to 33 wt.%, preferably 25 to 32 wt.%. The NCO content was determined by GB/T12009.4-2016.

B) Polyhydric alcohols

The polyol of the present invention may be a polyether polyol, a polyester polyol, a polycarbonate polyol and/or a mixture thereof.

The polyol of the present invention is preferably one or more polyether polyols, wherein at least one polyether polyol is an amine-initiated polyol. The polyether polyol has a functionality of 2 to 8, preferably 3 to 6, and a hydroxyl value of 50 to 1200, preferably 200 to 800.

The polyether polyols may be prepared by known processes. Ethylene oxide or propylene oxide is typically prepared with ethylene glycol, 1, 2-propylene glycol, 1, 3-propylene glycol, diethylene glycol, glycerol, trimethylolpropane, pentaerythritol, triethanolamine, toluenediamine, sorbitol, sucrose, or any combination thereof as a starter.

In addition, the polyether polyol can be prepared by reacting at least one alkylene oxide containing 2 to 4 carbon atoms with a compound containing 2 to 8, preferably, but not limited to, 3 to 8 active hydrogen atoms or other reactive compounds in the presence of a catalyst.

Examples of such catalysts are alkali metal hydroxides such as sodium hydroxide, potassium hydroxide, or alkali metal alkoxides such as sodium methoxide, sodium ethoxide or potassium isopropoxide.

Useful olefin oxides include, preferably but are not limited to, tetrahydrofuran, ethylene oxide, 1, 2-propylene oxide, 1, 2-butylene oxide, 2, 3-butylene oxide, styrene oxide, and any mixtures thereof.

Useful active hydrogen atom containing compounds include polyhydroxy compounds, preferably, but not limited to, water, ethylene glycol, 1, 2-propylene glycol, 1, 3-propylene glycol, diethylene glycol, trimethylolpropane, any mixture thereof, more preferably polyhydric, especially trihydric or higher alcohols, such as glycerol, trimethylolpropane, pentaerythritol, sorbitol and sucrose. Useful active hydrogen atom-containing compounds also include, preferably but not limited to, organic dicarboxylic acids such as succinic acid, adipic acid, phthalic acid and terephthalic acid, or aromatic or aliphatic substituted diamines such as ethylenediamine, diethylenetriamine, triethylenetetramine, propylenediamine, butylenediamine, hexamethylenediamine or toluenediamine.

Other reactive compounds that may be used include ethanolamine, diethanolamine, methylethanolamine, ethylethanolamine, methyldiethanolamine, ethyldiethanolamine, triethanolamine, and ammonia.

The polyether polyol prepared by using amine as a starter comprises a compound obtained by reacting amine as a starter with an alkylene oxide compound.

The term "alkylene oxide compound" as used in the present invention generally refers to compounds having the following general formula (I):

wherein R is₁And R₂Independently selected from H, C₁～C₆Straight and branched chain alkyl groups as well as phenyl and substituted phenyl groups.

Preferably, R₁And R₂Independently selected from H, methyl, ethyl, propyl and phenyl.

The person skilled in the art knows the preparation of "alkylene oxide compounds", which can be obtained, for example, by oxidation of alkylene compounds.

Examples of the alkylene oxide compounds useful in the present invention include, but are not limited to: ethylene oxide, 1, 2-propylene oxide, 1, 2-butylene oxide, 2, 3-butylene oxide, styrene oxide or mixtures thereof, with mixtures of ethylene oxide and 1, 2-propylene oxide being particularly preferred.

The term "alkylene oxide compound" as used in the present invention also includes oxacycloalkanes, examples of which include, but are not limited to: tetrahydrofuran and oxetane.

As used herein, the term "amine" refers to a compound containing a primary amino group, a secondary amino group, a tertiary amino group, or a combination thereof. Examples of compounds useful as amines in the present invention include, but are not limited to, triethanolamine, ethylenediamine, tolylenediamine, diethylenetriamine, triethylenetetramine, and derivatives thereof, preferably ethylenediamine, tolylenediamine, and particularly preferably tolylenediamine.

Examples of polyether polyols which can be used in the present invention are aromatic amine-initiated polyether polyols, preferably propylene oxide-based polyether polyols initiated with diphenylmethanediamine.

Preferably, the polyether polyols of the present invention include those having a functionality of from 2.0 to 8.0 and a hydroxyl number of from 50 to 550mg KOH/g, preferably from 90 to 450mg KOH/g (test method ISO 14900-2017).

Preferably, the component B further comprises at least one of the following components:

B1) polyether polyol having a functionality of not less than 4 and a hydroxyl number of < 400mg KOH/g (test method ISO 14900-2017), in an amount of from 5 to 45pbw, preferably from 7 to 25pbw, based on 100pbw of component B;

B2) polyether polyols having a functionality of > 4 and a hydroxyl number of > 400mg KOH/g (test method ISO 14900-2017) in an amount of from 20 to 70pbw, preferably from 30 to 65pbw, based on 100pbw of component B;

B3) an aromatic amine-initiated polyether polyol having a functionality of from 3.5 to 4.2, a hydroxyl number of < 400mgKOH/g (test method ISO 14900-2017) and a viscosity at 25 ℃ of < 30000 mPa.s (test method ISO 3219-1993), in an amount of from 5 to 35pbw, preferably from 10 to 20pbw, based on 100pbw of component B;

B4) polyether polyols having a functionality of < 3 and a hydroxyl number of < 400mg KOH/g (test method ISO 14900-2017) in an amount of from 0 to 15pbw, preferably from 3 to 10pbw, based on 100pbw of component B.

Foaming agent

The blowing agent of the present invention may be selected from various physical blowing agents and/or chemical blowing agents. Preferably, the content of the foaming agent is 2 to 30 wt.%, preferably 5 to 25 wt.%, based on the total weight of component B.

Useful blowing agents include water, halogenated hydrocarbons, and the like. Useful halohydrocarbons are preferably pentafluorobutane, pentafluoropropane, chlorotrifluoropropene, hexafluorobutene, HCFC-141 b (monofluorodichloroethane), HFC-365 mfc (pentafluorobutane), HFC-245 fa (pentafluoropropane), or any mixture thereof. Useful hydrocarbon compounds include preferably butane, pentane, Cyclopentane (CP), hexane, cyclohexane, heptane and any mixture thereof. Preferably, the blowing agent is selected from the group consisting of water, monofluorodichloroethane, cyclopentane, pentafluorobutane, pentafluoropropane, 1-chloro-3, 3, 3-trifluoropropene, 1-chloro-2, 3, 3, 3-tetrafluoropropene, hexafluorobutene, or combinations thereof. Preferably, the amount of water in the blowing agent is from 0.5 to 4.0% by weight, preferably from 1.0 to 2.5% by weight, based on 100% by weight of the total weight of component B.

Catalyst and process for preparing same

The polyurethane reaction system of the present invention also includes catalysts including blowing catalysts, gelling catalysts, and trimerization catalysts.

Preferably, the foaming catalyst is selected from one or a mixture of pentamethyldiethylenetriamine, bis-dimethylaminoethylether, N, N, N '-tetramethylethylenediamine, N, N, N' -tetramethylbutanediamine and tetramethylhexanediamine in any proportion; the gel catalyst is selected from one or a mixture of two of dimethylcyclohexylamine and dimethylbenzylamine in any proportion; the trimerization catalyst is selected from one or more than one of methyl ammonium salt, ethyl ammonium salt, octyl quaternary ammonium salt or hexahydro triazine and organic metal alkali in any proportion.

In an embodiment of the present invention, the polyurethane reaction system of the present invention further comprises water, wherein the moisture content is: 0.1 to 3.5 wt.%, preferably 0.5 to 2.8 wt.%, particularly preferably 1.5 to 2.6 wt.%, based on the total weight of component B, excluding the blowing agent.

The polyurethane reaction system of the present invention also includes at least one flame retardant in an amount of 5 to 25pbw, preferably 10 to 20pbw, based on 100pbw of component B. The flame retardant of the present invention includes halogen flame retardants and non-halogen flame retardants.

In embodiments of the present invention, the reactive system of the polyurethane foam of the present invention further comprises a surfactant/foam stabilizer, preferably, but not limited to, ethylene oxide derivatives of siloxanes. The surfactants are used in amounts of 0.1 to 5.0 wt.%, preferably 0.5 to 4.0 wt.%, particularly preferably 1.5 to 3.0 wt.%, based on the total weight of component B, in 100 wt.%.

Through experiments, we unexpectedly found that the method for preparing rigid polyurethane foam of the present invention successfully reduces the thermal conductivity of rigid polyurethane foam and enhances other physical properties. Specifically, the thermal conductivity of the rigid polyurethane foam obtained by foaming the mold at an angle of 0 degrees or more to the horizontal plane at 25 ℃ is decreased by not less than 1%, preferably not less than 2%, more preferably not less than 3%, particularly preferably not less than 5% as compared with the case where the mold is at an angle of 0 degrees to the horizontal plane at the time of foaming the polyurethane reaction system (test method ASTM C177-2010).

It is known to those skilled in the art that the polyurethane reaction system pouring gate is typically located at the top of the mold. If the mould is inclined at a certain angle during foaming, the polyurethane reaction system is poured from the top, and liquid of the polyurethane reaction system is always splashed to the inner wall of the mould, so that uneven foaming is caused. We tried to place the gate lower near the horizontal plane of the mold, and surprisingly, solved this problem. Furthermore, even more surprisingly, when the pouring gate is provided at 1/2 or less, preferably 1/3 or less, and more preferably 1/4 or less, near the horizontal plane in the height direction of the mold, we have found that it is also possible to improve the predistribution of the reaction materials in the mold and thus to improve the heat insulating properties of the rigid polyurethane foam. On the contrary, if the raw materials of the reaction system are not injected from the lowest part of the mold, the reaction raw materials firstly flow to the bottom of the mold from a certain height and then are inspired to fill the mold, so that the foam pores are influenced in the flowing process of the raw materials, and the heat insulation performance of the foam is deteriorated.

The method of the invention is simple and easy to operate, does not need to increase expensive equipment investment, and is very beneficial to the production of heat insulation equipment.

Polyurethane foam

In the embodiment of the present invention, it is preferable that the core density of the rigid polyurethane foam is 30-80kg/m3, preferably 35-65kg/m3 (test method ISO 845-2006).

Preferably, the thermal conductivity coefficient of the rigid polyurethane foam at 25 ℃ is less than or equal to 23.80mW/m^＊K, preferably ≤ 23.70mW/m^＊K, more preferably not more than 23.60mW/m^＊K (test method ASTM C177-2010).

The polyurethane foam of the present invention can be used to prepare polyurethane composite panels. The polyurethane composite board of the invention can be composed of two surface layers and a polyurethane foam layer positioned between the two surface layers.

Preferably, the two face layer materials of the composite plate are selected from one or more of iron, aluminum, FRP, PS and ABS.

The method for preparing the polyurethane composite board comprises the following steps:

fixing the two surface layers; and

and injecting a polyurethane reaction system between the two surface layers, and carrying out reaction foaming molding on the polyurethane reaction system to obtain the polyurethane composite board.

Preferably, the two surface layers are fixed by a mold, the mold comprises an upper cover and a lower cover, and the two surface layers are respectively fixed on the inner surface of the upper cover and the inner surface of the lower cover.

The two surface layers in the method for preparing the polyurethane composite board are preferably fixed by a mould, the mould comprises an upper cover and a lower cover, and the two surface layers are respectively fixed on the inner surface of the upper cover and the inner surface of the lower cover.

The method for preparing the polyurethane composite board preferably uses a discontinuous production process. The composite plate generally includes a cavity and polyurethane foam filled in the cavity, and the cavity is made of metal, plastic, composite plate, and the like. The hollow shell can be prefabricated, then the joint of the hollow shell is sealed, the glue injection hole and the exhaust hole are reserved, finally the hollow shell is placed in a foaming forming mould, and the polyurethane composition is applied to the cavity of the hollow shell through the mould and the glue injection hole of the hollow shell. And after the foaming reaction of the polyurethane composition is finished, taking the foamed workpiece out of the mold to obtain the polyurethane composite material.

In some embodiments of the invention, the cavity has a plate-like, U-shaped or hollow cylindrical shape.

The rigid polyurethane foam of the invention is mainly applied to the preparation of heat insulation equipment. In other embodiments of the present invention, the polyurethane composite prepared by the discontinuous process is applied to home appliances such as refrigerators, freezers, refrigerated vehicles, water heaters, holding tanks, incubators, heat shields, and the like.

The heat insulation equipment comprises the polyurethane foam or the polyurethane composite board. The heat insulation equipment can be a refrigerator, an ice chest, a fridge, a refrigerator car, a water heater, a heat preservation barrel, a heat preservation box, a heat insulation box and the like.

Examples

Description of raw materials:

DC380, polyether polyol, available from sentenc nigung new materials development ltd, hydroxyl number: 380, viscosity 11250, functionality 5.8;

NJ8268, polyether polyol, available from sentenc Ningwu New Material development ltd, hydroxyl number: 310, viscosity 1200, functionality 4.0;

NJ8345, polyether polyol, available from sentencing new materials development ltd, hydroxyl number: 450, viscosity 17000, functionality 5.2;

DC635C, polyether polyol, available from sentencing niu new materials development ltd, hydroxyl number: 500, viscosity 5800, functionality 4.5;

z450, polyether polyol, available from costa creative taiwan limited, hydroxyl number: 345, viscosity 12000, functionality 4.0;

TCPP, halogen flame retardant, available from yake science ltd, jiang su;

TEP, a non-halogen flame retardant, available from yack science ltd, jiang su;

l6920, foam stabilizer, available from mai chart advanced materials (china) ltd;

cyclopentane, a blowing agent, available from maylon, guangzhou;

HFC 245fa and LBA, available from Honeywell corporation;

dabco Polycat 41, a polyurethane synthesis catalyst, available from air chemical products (China) Inc.;

dabco polycat8, a polyurethane synthesis catalyst, available from air chemical products (China) Inc.;

44v20L, isocyanate, NCO content 31.5 wt.%, available from kostew polymers (china) ltd.

The test method comprises the following steps:

testing the physical properties of the foam: putting a kraft paper box into a mold with a certain size, controlling the temperature of the mold at a set value, injecting a set amount of foam reaction raw materials, taking out the foam after the foam is solidified, and testing the density, the compressive strength and the heat conductivity coefficient of the foam core after the foam is placed for 24 hours in an environment with the temperature of 23 ℃ and the humidity of 50%.

And (4) testing the compression strength according to the GB8813 standard.

Thermal conductivity, according to ASTM C177-2010.

Preparation of rigid polyurethane foams

The components B shown in the table 1 are uniformly stirred according to the proportion for later use, and the cyclopentane parts shown in the table 2 are added and uniformly stirred. The prepared raw materials (components A and B) were kept at a temperature of 20 ℃ in an incubator until use. The specific angles of the examples or comparative examples shown in tables 2 and 3 are respectively adjusted, then A and B (containing foaming agent) are uniformly stirred (stirring time is 10 seconds, stirring speed is 4000 rpm) according to the proportion shown in tables 2 and 3 and poured into a mold, when the specified demolding is reached, the mold can be opened, the foamed and molded plate can be taken out, and the next procedure is carried out.

TABLE 1 polyurethane reaction System component B the respective component ratios (unit: pbw, water wt%)

Effect of foaming Angle on foam Properties

TABLE 2 influence of reaction System # 1 foaming Angle on foam Performance

TABLE 3 influence of the foaming Angle on the foam Properties of the reaction System # 2

From the experimental results of tables 2 and 3, it is understood that the thermal conductivity of the rigid polyurethane foam obtained by foaming the mold at a certain angle, for example, 10 ° or more, to the horizontal plane at the time of foaming the polyurethane reaction system is remarkably reduced, as compared with the case where the angle of the mold to the horizontal plane at the time of foaming the polyurethane reaction system is 0 °. Specifically, the thermal conductivity of the rigid polyurethane foam obtained by foaming the polyurethane reaction system at a certain angle to the horizontal plane is reduced by not less than 1%, preferably not less than 2%, more preferably not less than 3%, and particularly preferably not less than 5% at 25 ℃ as compared with the case where the angle of the mold to the horizontal plane is 0 degree when the polyurethane reaction system is foamed (test method ASTM C177-2010).

TABLE 4 influence of reaction System # 1-injection position on foam Performance

From the experimental data in Table 4, it can be seen that the injection location has some effect on the foam performance, i.e., the thermal conductivity of the foam decreases significantly when the injection is at a height below 1/2. If the foaming angle is kept unchanged, and the position of the injection port is only changed, the physical properties of the obtained foam are not greatly different, but the heat conductivity coefficient is obviously changed. As the sprue height decreases at the die, the thermal conductivity of the foam decreases.

Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes and modifications can be made therein by those skilled in the art without departing from the spirit and scope of the invention as defined by the appended claims.