CN1422292A - Polyurethane foams with reduced exothermy - Google Patents

Polyurethane foams with reduced exothermy Download PDF

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Publication number
CN1422292A
CN1422292A CN01807891A CN01807891A CN1422292A CN 1422292 A CN1422292 A CN 1422292A CN 01807891 A CN01807891 A CN 01807891A CN 01807891 A CN01807891 A CN 01807891A CN 1422292 A CN1422292 A CN 1422292A
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component
foams
acid
polyol
prepolymer
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CN01807891A
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CN1167723C (en
Inventor
T·弗里克
E·-M·霍佩
M·卡普斯
F·梅耶
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Rock & Co Ltd
Bayer AG
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Rock & Co Ltd
Bayer AG
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K17/00Soil-conditioning materials or soil-stabilising materials
    • C09K17/14Soil-conditioning materials or soil-stabilising materials containing organic compounds only
    • C09K17/18Prepolymers; Macromolecular compounds
    • C09K17/30Polyisocyanates; Polyurethanes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00Foam properties
    • C08G2110/0083Foam properties prepared using water as the sole blowing agent

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Soil Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)

Abstract

The invention concerns polyurethane foams with reduced exothermy and to the use thereof for hardening rocks in mining and underground engineering.

Description

The urethane foam of low exothermicity
The present invention relates to the urethane foam system of low exothermicity and relate to they solidify the geology formulation in underground mining, in tunnel construction and in underground works (Tiefbau) purposes.
Two component polyurethane foams system is used at coal mining consolidated rock and coal and is used for sealing going into flowing water with opposing to a great extent.Is heat release from polyisocyanates and polyvalent alcohol formation urethane in principle.Under adverse environment, because the high reaction temperature that produces in foam makes coal dust on fire.Especially when reaction mixture flows in the big relatively spacious space, the core temperature of urethane foam can be brought up to spontaneous combustion that urethane takes place and the therefore a kind of degree of coal combustion in-situ of making.
For fear of this shortcoming of polyurethane system, EP-A 167 002 has advised using the reaction product of isocyanic ester and alkali metal silicate aqueous solution.EP A 636 154 discloses by polyisocyanates, the reaction of alkali metal silicate aqueous solution and cement.Yet these systems can't be succeedd in practice.
Have now found that by by some polyisocyanate prepolymers and selected polyvalent alcohol and appropriate filler blending, the heat release that urethane forms can be reduced to a kind of degree that no longer includes hazard of catch fire in the consolidation process of rock.
So, the present invention relates to contain polyurethanyl group and the foams that reaction obtained by following component:
1. have 20-30wt.%, the polyisocyanate component of the NCO content of preferred 23-28wt.%, it comprises the prepolymer that contains isocyanate group of the NCO content with 20-28wt% of 50wt.% at least,
2. have 120 to 350, the polyol component of preferred 180 to 300 OH value,
3. be dispersed in polyol component b) or prepolymer a) in, preferably at polyol component b) in, and have 4-100 μ m, preferred 4-25 μ m, the solid packing of 10-25 μ m mean particle size especially,
4. water,
5. Ren Xuan catalyzer,
6. Ren Xuan additional additives.
According to the present invention, this isocyanate component a) contains 20-30wt.%, the NCO group of preferred 23-28wt.% and contain 50wt.% at least contain 20-30wt.%, the prepolymer of the isocyanate group of preferred 23-28wt.%.Preferably by the isocyanic ester and functionality and 350-1 with 3-8 of diphenylmethane series, 000 OH value and 150-1, the polyether polyol of 000 number-average molecular weight react prepared to this prepolymer.Suitable prepolymer also is described among the EP-A 550 901.The isocyanic ester of employed diphenylmethane series is two nuclear diphenylmethanediisocyanates, as 4,4 '-and/or 2,4 '-diphenylmethanediisocyanate of ditan-vulcabond or their more higher homologue or two or more nuclears for example the mixture or have of polyphenylene polymethylene polyisocyanates (as by aniline-formaldehyde condensation reaction and the prepared product (" thick MDI ") of phosgenation subsequently) be higher than the industrial polyisocyanates (commodity are called " polymerization ditan-vulcabond ") that obtains of 2.0 functionality.
The product that comprises two nuclear isomers of 75-95wt% is preferred, especially in two nuclear isomers 2,4 '-content of isomer is that 15-40wt.% and 2,2 '-content of isomer is those products of 2-10wt%.
Except that prepolymer, this isocyanate component a) can comprise other isocyanic ester of the diphenylmethane series of 50wt% at the most.This is polymeric MDI preferably.Yet monomer M DI also can use, or the MDI type that is modified, and those that for example contain biuret, allophanate and isocyanurate group can use, if isocyanate component viscosity a) be unlikely raise too many.
In order to ensure isocyanate component good workability a), its viscosity preferably is adjusted at 200-6,000mPas, and preferred especially 500-3 is in the 000mPas scope.This type of isocyanate component can be usually used in the piston or the toothed gear pump of fixed rock mass by use, without any problem be transferred and inject the rock mass layer.
Polyol component b) has 120 to 350, preferred 180 to 300 OH value.This polyol component preferably comprise have 2-8, the functionality of preferred 2-4 and by alkylene oxide such as oxyethane, propylene oxide, butylene oxide ring, decyl oxyethane or phenyl ethylene oxide, the polyoxyalkylene polyol that optimization ethylene oxide and/or propylene oxide, addition polymerization are obtained to the initiator compound with active hydrogen atom.Employed initiator compound is the compound with two or more terminal hydroxy groups, for example, and water, trolamine, 1,1,2-propylene glycol, 1, ammediol, glycol ether, dipropylene glycol, triglycol, tripropylene glycol, 1,2-butyleneglycol, 1,3 butylene glycol, 1,4-butyleneglycol, 1,2-hexylene glycol, 1, the 3-hexylene glycol, 1,4-hexylene glycol, 1,5-hexylene glycol, 1,6-hexylene glycol, glycerine, TriMethylolPropane(TMP), tetramethylolmethane and Sorbitol Powder.These initiator compounds can use separately or use as mixture.
One or more polyester polyols also can be with components b) the amount of 10wt.% at the most of total amount be used for polyol component b jointly).Suitable polyester polyol has 200-6,000g/mol, and preferred 200-2, the number-average molecular weight of 400g/mol, and can obtain with the polyvalent alcohol that contains at least two hydroxyls from aromatics and/or aliphatic dicarboxylic acid.The example of dicarboxylic acid is a phthalic acid, m-phthalic acid, terephthalic acid, fumaric acid, toxilic acid, nonane diacid, pentanedioic acid, hexanodioic acid, suberic acid, sebacic acid, propanedioic acid and succsinic acid.Can use pure dicarboxylic acid and their any desirable mixture.The dicarboxylic acid that need not dissociate also can use corresponding dicarboxylic acid derivatives, for example has the dicarboxylic acid list or the diester class of the alcohols of 1-4 carbon atom.This type of ester class for example forms in the recycling of polyester waste material.Dicarboxylic anhydride as Tetra hydro Phthalic anhydride or maleic anhydride, also can be used as acid constituents.Following compound is preferably used as the alkoxide component of esterification: ethylene glycol, glycol ether, Tetraglycol 99,1,2-propylene glycol, 1, ammediol, 1,4-butyleneglycol, 1,5-pentanediol, 1,6-hexylene glycol, decamethylene-glycol, glycerine, TriMethylolPropane(TMP), tetramethylolmethane or their mixture.Also might use from lactone for example 6-caprolactone, or hydroxycarboxylic acid, for example polyester polyol of 'omega '-hydroxy carboxylic acid formation.This polyol component can also comprise the polyether ester polyvalent alcohol, can and obtain with reacting ethylene oxide subsequently by Tetra hydro Phthalic anhydride and glycol ether reaction as it.
In the preparation of foams of the present invention, have 4-100 μ m, preferred 4-25 μ m, especially the solid packing of the mean particle size of 10-25 μ m is as amount of component b).Package stability dispersion with the viscosity that is suitable for processing can obtain with this filler.Appropriate filler is, for example, and three aluminium hydroxides, the urea-formaldehyde resin (condensation product of urea and formaldehyde, referring to Houben-Weyl, " Methoden der organi schen Chemie[organic chemistry method] ", the XIV volume, 1963, the 319-402 page or leaf), rock dust or pyrogenic silica; Three aluminium hydroxides are preferred.In order to prepare according to foams of the present invention, filler is dispersed or suspended in polyol component b) or prepolymer a) in, preferably at polyol component b) in.This filler is preferably with 30-55wt.%, and the amount of preferred especially 35-50wt.% is used, based on the amount of suspension agent.
If this filler is dispersed in polyol component b) in, the viscosity that then contains the polyol component of filler should preferably be no more than 6,000mPas, and they can utilize low-pressure pump to carry like this.The viscosity of isocyanate component and the polyol component that contains filler especially preferably is adjusted to approximately identical value, in order that help processing, the especially uniform mixing of each component.
In order to prepare foams of the present invention, water is as whipping agent d), preferably with 0.1-1wt%, the amount of preferred especially 0.6-0.9wt% is added, based on this polyol component b).Most preferably, the amount of water makes the foaming coefficient (Sch  umfaktor) that reaches 2-6 through calculating the back, that is, the volume of prepared foams be starting ingredient cumulative volume 2-6 doubly.
In the preparation process of foams of the present invention, can randomly add and to quicken catalyst for reaction e between isocyanate component and polyol component).The example of suitable catalyst is an organo-tin compound, tin (II) salt as organic carboxylic-acid, tin acetate (II) salt for example, stannous octoate (II), thylhexoic acid tin (II) and tin laurate (II), and dialkyl tin (IV) salt, for example dibutyltin diacetate, dibutyl tin dilaurate and oxalic acid dioctyl tin.Other example of suitable catalyst is an amine, as the dimethylaminopropyl urea, and dimethylaminopropyl amine, two (dimethylaminopropyl) amine, diazabicyclo octane, dimethylethanolamine, triethylamine, dimethylcyclohexylam,ne, dimethyl benzyl amine, five methyl diethylentriamine, N, N, N ', N '-tetramethyl butane diamine, N-methylmorpholine, two (dimethyl aminoethyl) ethers and three (dialkyl aminoalkyl)-s-Hexahydrotriazines.
The example of producing the suitable catalyst of polyisocyanic acid ester structure is a sylvite, as potassium acetate or potassium octanoate.Also can use several mixture of catalysts.
Optional also have other additive f) be used for preparation according to foams of the present invention, pigment for example, dyestuff or softening agent are as dioctyl phthalate (DOP).These are usually with the 0-10 weight part, and the amount of preferred 0-5 weight part joins in the polyol component.
The also optional fire retardant that adds, preferably liquid and/or can dissolved in one or more of the component that is used for preparing foams those.Commercially available phosphonium flame retardant is preferred the use, lindol for example, tricresyl phosphate (2-chloropropyl) ester, tricresyl phosphate (2, the 3-dibromopropyl) ester, tricresyl phosphate (1,3-two chloropropyls) ester, bisphosphate four (2-chloroethyl) ethylidene ester, diethyl ethane phosphonic acid ester and diethanolamine ylmethyl diethyl phosphonate.Have fire retardation halogen-containing-and/or phosphorous-polyvalent alcohol also be suitable.Fire retardant is preferably with maximum 35wt.%, and the amount of preferred especially maximum 20wt.% is used, based on components b).
The present invention also provide foams of the present invention in mining and underground works, be used for rock fixed, for example be used for coal and rock fixed on every side and be used to seal to resist the various uses of underground hard coal mining inflow water.
Because geological fault section (St rungszonen) and by extracting caused hollow space out, rock avalanche from the wall has caused the serious interruption of producing and has caused sizable danger to the people of underground operation.
In the consolidation process of rock mass, urethane foam according to the present invention utilizes suitable syringe pump to flow in the fixed rock mass layer of needs via boring.The expansible reaction mixture makes the slit of filling and crack that gluing take place, and therefore causes forming once more the system strength of geology series of rocks; Rock or coal fall can prevent reliably.
According to the preparation of foams of the present invention preferably by with isocyanate component a) and comprise components b), c), d), e) and f) mixture mix by 1: 1 volume ratio and carry out.Preferably be defined as the NCO/OH ratio of 130-300 here, preferred especially 180-260.
The preferred prescription of selecting according to foams of the present invention makes the temperature that reaction mixture reached in the urethane forming process be no more than 120 ℃ top temperature.It is particularly preferred that maximum temperature is no more than 110 ℃ prescription.
Embodiment
Following starting ingredient is used for the following example:
Formulation A
Have the polyol blends of the OH value of 239mg KOH/g, form by following component: the 1) polyethers with OH value 190 of 20.9 weight parts, it is obtained by propylene glycol and reacting ethylene oxide,
2) polyethers with OH value 255mg KOH/g of 78 weight parts, it is obtained by TriMethylolPropane(TMP) and oxyethane and propylene oxide reaction,
3) 0.9 weight part as the water of whipping agent and
4) dibutyl tin laurate as catalyzer of 0.2 weight part.
Formulation B
Have the polyol blends of the OH value of 111mg KOH/g, form by following component:
1) polyethers with OH value 112 of 98.9 weight parts, it is obtained by propylene glycol and propylene oxide reaction,
2) 0.9 weight part as the water of whipping agent and
3) dibutyl tin laurate as catalyzer of 0.2 weight part.
Formulation C
Have the polyol blends of the OH value of 381mg KOH/g, form by following component:
1) polyethers with OH value 385 of 98.9 weight parts, it is obtained by TriMethylolPropane(TMP) and propylene oxide reaction,
2) 0.9 weight part as the water of whipping agent and
3) dibutyl tin laurate as catalyzer of 0.2 weight part.
Formulation D
Have the polyol blends of the OH value of 242mg KOH/g, form by following component:
1) polyethers with OH value 245 of 98.9 weight parts, it is obtained by glycerine and propylene oxide reaction,
2) 0.9 weight part as the water of whipping agent and
3) dibutyl tin laurate as catalyzer of 0.2 weight part.
Isocyanic ester I
Isocyanate prepolymer (Desmodur with NCO content of 25.6wt.% VP.PU28HS07, Bayer AG, D-51368 Leverkusen); Contain 4 of 60wt.%, 2 of 4 '-two isocyano ditans and 22wt.%, 4 '-two isocyano ditans, with 2 of 3wt.%, the polyisocyanates of 2 '-two isocyano ditans is and by TriMethylolPropane(TMP) and propylene oxide reaction obtained, have OH value 865 the polyether polyol reaction product according to the amount ratio of 92.5wt%MDI/7.5wt% polyvalent alcohol.
Isocyanic ester II
Polyisocyanates (Desmodur with NCO content of 31wt% 44V70 L, BayerAG, D-51368 Leverkusen), it comprises the two isocyano ditan isomer of about 31wt.%, and wherein about 89wt.% is that 4,4 '-two isocyano ditans and about 11wt.% are 2,4 '-two isocyano ditans.
Aluminium hydroxide (Martinal with mean particle size of 15-25 μ m ON-320, Martinswerk GmbH, D-50127 Bergheim) as solid matter (Feststoff).
These components are tested in the laboratory by known way: these components of about 200 grams are according to 1: 1 volume ratio of isocyanic ester and polyvalent alcohol and mix under 23 ℃ material temperature.This temperature of reaction of middle measurements at sample.After about four hours, the cropped and assess foam structure of sample.
Test-results is shown in the following table 1.
Table 1
Embodiment ????1 ????2 * ????3 * ????4 ????5 ????6 * ????7 * ????8
Polyol component
A[weight part] ????55 ????- ????- ????- ????75 ????100 ????55 ????55
B[weight part] ????- ????55 ????- ????- ????- ????- ????- ????-
C[weight part] ????- ????- ????55 ????- ????- ????- ????- ????-
D[weight part] ????- ????- ????- ????55 ????- ????- ????- ????-
Isocyanate component
I[weight part] ????90 ????90 ????90 ????90 ????90 ????90 ????- ????45
II[weight part] ????- ????- ????- ????- ????- ????- ????90 ????45
The OH value of polyol component [mg KOH/g] ????239 ????111 ????381 ????242 ????239 ????239 ????239 ????239
The NCO content [wt.%] of isocyanate component ????25.6 ????25.6 ????25.6 ????25.6 ????25.6 ????25.6 ????31.0 ????28.1
????Al(OH) 3[wt.%] ????45 ????45 ????45 ????45 ????25 ????0 ????45 ????45
Foam structure ????A ????K ????A ????A ????A ????A ????K ????A
Maximum temperature [℃] ????105 ????68 ????131 ????103 ????115 ????121 ????97 ????99
*Not according to comparative example of the present invention
A: acceptable, K: subside

Claims (3)

1. the foams that contain polyurethanyl group can be obtained by following component reaction:
A) have the polyisocyanate component of the NCO content of 20-30wt.%, it comprises the prepolymer that contains isocyanate group of the NCO content with 20-28wt% of 50wt.% at least,
B) have the polyol component of 120 to 350 OH value,
C) be dispersed in polyol component b) or this prepolymer a) in and solid packing with 4-100 μ m mean particle size,
D) water,
E) Ren Xuan catalyzer,
F) Ren Xuan additional additives.
2. according to the preparation method of the foams that contain polyurethanyl group of claim 1, wherein isocyanate component a) with comprise components b), c), d) and optional e) and mixture f) react by 1: 1 volume ratio.
3. be used for purposes according to the foams of claim 1 at mining and underground works consolidated rock.
CNB018078915A 2000-04-13 2001-04-02 Polyurethane foams with reduced exothermy Expired - Fee Related CN1167723C (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10018395A DE10018395B4 (en) 2000-04-13 2000-04-13 Low exothermic polyurethane foams
DE10018395.6 2000-04-13

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CN1167723C CN1167723C (en) 2004-09-22

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HK (1) HK1054559B (en)
PL (1) PL206612B1 (en)
UA (1) UA73564C2 (en)
WO (1) WO2001079321A1 (en)
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019001838A (en) * 2017-06-12 2019-01-10 旭有機材株式会社 Agent liquid composition for grouting
CN110790883A (en) * 2019-11-15 2020-02-14 上海东大聚氨酯有限公司 Low-heat-release combined polyether, polyurethane raw material composition, polyurethane foam and preparation method thereof

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Publication number Priority date Publication date Assignee Title
US20070093602A1 (en) * 2005-10-24 2007-04-26 Bayer Materialscience Llc Solid polyurethane compositions, infrastucture repair and geo-stabilization processes
CN102226088B (en) * 2011-04-27 2013-03-06 南京大学 Polyurethane-based ecological sand-fixing agent and preparation method thereof
CN102251517B (en) * 2011-04-27 2013-03-13 南京大学 Dust prevention and sand fixation method
EP2706148B1 (en) 2012-08-30 2014-10-15 TuTech Innovation GmbH Method for improving the bearing capacity of open profiles placed in the foundation and system created using the same
AU2020220093A1 (en) * 2019-08-26 2021-03-18 Gcp Applied Technologies Inc. Penetrating single component prepolymer system

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DE1159865B (en) * 1962-10-31 1963-12-19 Peute Chemie G M B H & Co Kg Procedures and sealing and consolidation of geological formations
CA999400A (en) * 1972-04-28 1976-11-02 General Tire And Rubber Company (The) Flame retardant flexible polyurethane foams
US4114382A (en) * 1974-07-26 1978-09-19 Bayer Aktiengesellschaft Process for the consolidation of geological formations and loosened rock and earth masses
DE2524191C3 (en) * 1975-05-31 1980-04-03 Bayer Ag, 5090 Leverkusen Process for the production of hole-filled lightweight foams containing hydrophobic urea groups
US4454252A (en) * 1981-03-02 1984-06-12 Bergwerksverband Gmbh Process of sealing and strengthening water-bearing geological formations by means of polyurethane-resin-forming compositions
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DE3704802A1 (en) * 1987-02-16 1987-10-08 Horst Ing Grad Kaiser Process for modifying the mechanical properties of polyurethane foams

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019001838A (en) * 2017-06-12 2019-01-10 旭有機材株式会社 Agent liquid composition for grouting
CN110790883A (en) * 2019-11-15 2020-02-14 上海东大聚氨酯有限公司 Low-heat-release combined polyether, polyurethane raw material composition, polyurethane foam and preparation method thereof
CN110790883B (en) * 2019-11-15 2021-11-23 上海东大聚氨酯有限公司 Low-heat-release combined polyether, polyurethane raw material composition, polyurethane foam and preparation method thereof

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PL206612B1 (en) 2010-08-31
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DE10018395A1 (en) 2001-10-31
ZA200207411B (en) 2003-09-16
DE10018395B4 (en) 2004-07-15
AU6017501A (en) 2001-10-30
PL358663A1 (en) 2004-08-09
HK1054559B (en) 2005-05-27
CN1167723C (en) 2004-09-22
HK1054559A1 (en) 2003-12-05
AU2001260175B2 (en) 2005-07-21

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