CN1290898C - Method for preparing polyether glycol in use fire resistant hard foam of polyurethane - Google Patents
Method for preparing polyether glycol in use fire resistant hard foam of polyurethane Download PDFInfo
- Publication number
- CN1290898C CN1290898C CN 200510045791 CN200510045791A CN1290898C CN 1290898 C CN1290898 C CN 1290898C CN 200510045791 CN200510045791 CN 200510045791 CN 200510045791 A CN200510045791 A CN 200510045791A CN 1290898 C CN1290898 C CN 1290898C
- Authority
- CN
- China
- Prior art keywords
- parts
- reaction
- polyurethane
- fire resistant
- temperature
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Polyurethanes Or Polyureas (AREA)
- Polyethers (AREA)
Abstract
The present invention relates to a preparation method for polyether polyhydric alcohol for a polyurethane hard bubble with high temperature resistance, which is characterized in that the preparation method comprises the following steps: 24 to 31 parts by weight of initiator and 0.1 to 0.5 part by weight of alkali metal hydroxide solution as a catalyst are added into a reaction kettle, the reaction kettle is evacuated, deoxidated and filled with nitrogen, and the initiator and the catalyst are stirred to be heated to 80 to 100 DEG C; oxyalkylene accounts for 30% of total amount is put into the reaction kettle; reaction temperature is from 80 to 100 DEG C, pressure is from 0.2 to 0.8MPa, and reaction time is from 2 to 3 hours; temperature is raised to 100 to 130 DEG C, residual oxyalkylene is added after vacuum dehydration, and reaction is carried out for 4 to 7 hours; the twice adding total amount of the oxyalkylene is from 68.5 to 75.9 parts by weight; the neutralizer solution of the mixture of sodium acid pyrophosphate and phosphoric acid is adopted to carry out neutralization, neutralization temperature is from 120 to 130 DEG C, and neutralization time is 1.5 hours; moisture in reactants is eliminated, magnesium hexasilicate as an adsorbing agent which is 0.5 wt% of the total weight of materials is added to carry out adsorption for 0.5 hour, and potassium and sodium ions are removed; impurities are filtered, and a yellow viscous product is obtained. A hard bubble of the present invention has favorable size stability and temperature resistance, and can be suitable for an occasion of-30 DEG C to 150 DEG C. Energy is saved, and consumption is lowered. The yellow viscous product has the advantages of good quality and low cost.
Description
(1) technical field
The present invention relates to a kind of preparation method of polyurethane synthetic material, specifically relate to a kind of preparation method of polyether glycol in use fire resistant hard foam of polyurethane.
(2) background technology
Rigid urethane foam with its excellent material property and processing characteristics and relative cheap price advantage thereof, develops rapidly in novel synthetic material.Because development of new techniques and the requirement of being devoted to energy-conservation aspect, the sales volume that is used for lagging material just increases rapidly.But the finished product of the general rigid-foam polyether of domestic production, only be applicable to that the environment below 100 ℃ uses, use as long term high temperature, its performance significantly reduces, the basic dependence on import of polyethers that requires aspects such as higher heating power line of pipes insulation of use temperature and high-temperature disinfection cabinet to use.
External early seventies, the sorbyl alcohol polyethers EL-500S of Japan AGC company, viscosity is up to 30000CP/25 ℃, and is poor with the intermiscibility of other auxiliary agent, mobile bad, influenced use.
The LMP-320 of China Liaoning chemical research institute development is a kind of aromatic hydrocarbons polyethers, with hard bubbling of this polyethers production, though temperature tolerance improve and improve, the fragility height, physical strength is bad, and polyvalent alcohol viscosity is big.
(3) summary of the invention
The purpose of this invention is to provide that a kind of production technique is simple, production cost is low, the preparation method of modest viscosity, polyether glycol in use fire resistant hard foam of polyurethane that mechanical workout intensity is good.
The technical solution used in the present invention is: the preparation method of polyether glycol in use fire resistant hard foam of polyurethane, comprise with the polyol being initiator, and under catalyst action, the ring-opening polymerization of olefin oxide monomer.
Above-mentioned initiator comprises ethylene glycol, propylene glycol, glycerol, butyleneglycol, TriMethylolPropane(TMP), pentanediol, tetramethylolmethane, 1,2,6 ,-hexanetriol, sorbyl alcohol, Xylitol, N.F,USP MANNITOL, sucrose, glycerine, methyl glucoside make the Polyetherfunctional degree between 4～6.
Above-mentioned olefin oxide compounds comprises ethylene oxide, propylene oxide; Wherein the olefin oxide add-on should make the pfpe molecule amount be controlled in 400～800 scopes;
Above-mentioned polymerizing catalyst generally adopts alkali metal hydroxide, and comprising potassium hydroxide or sodium hydroxide, its content accounts for 0.1%～0.5% (weight) of product polyether glycol in use fire resistant hard foam of polyurethane total amount;
Above-mentioned polymerization temperature generally is controlled between 80 ℃～130 ℃; Polymerization pressure generally is controlled at 0.2～0.8Mpa, is 0.4～0.6MPa between dominant area; Polymerization time 6～10 hours, preferred 6～8 hours; Product polyether glycol in use fire resistant hard foam of polyurethane hydroxyl value is 400～500mg KOH/g, viscosity (25 ℃) 2500～5000CP, molecular weight 400～800.
The preparation method of polyether glycol in use fire resistant hard foam of polyurethane comprises the following steps:
A, reinforced: will be 24～31 parts initiator by weight, 0.1～0.5 part alkali hydroxide soln catalyzer, concentration is 30%～60%, join in the reactor, vacuumize deoxidation, fill nitrogen, pressure is opened stirring and is warming up to 80～100 ℃ less than 0.1Mpa;
B, polymerization: the olefin oxide that will account for total amount 30% drops in the still 80～100 ℃ of temperature of reaction, pressure 0.2～0.8MPa, 2～3 hours reaction times; Be warming up to 100～130 ℃, after the vacuum hydro-extraction, add remaining olefin oxide, reacted 4～7 hours; It is 68.5～75.9 parts that olefin oxide adds total amount twice;
C, neutralization: adopt the mixture neutralizing agent solution neutralization of Disodium pyrophosphate and phosphoric acid, 120～130 ℃ of neutral temperatures, 1.5 hours time;
D, dehydration and absorption: remove moisture in the reactant, add with the material gross weight than being 0.5% hexa-magnesium silicate adsorbents adsorb 0.5 hour, remove potassium, sodium ion;
E, filtration: elimination impurity promptly gets yellow thick product;
Advantage of the present invention is:
Composite by initiator, as to make polyethers modest viscosity has good intermiscibility with other auxiliary agent, and the feed liquid good fluidity is easy to foaming operation;
Hard bubbling has dimensional stability and temperature tolerance preferably, applicable to-30 ℃～150 ℃ occasions;
Energy-saving and cost-reducing, good product quality, cost is low.
(4) specific embodiment
Embodiment one
In the autoclave that has whipping appts and inner coil refrigerating unit, drop into 13.7 parts of sorbyl alcohols, 9.7 parts of sucrose, 5.7 parts of glycerine, 0.23 part of potassium hydroxide solution, concentration is 48%, vacuumizes deoxygenation.Open stirring, be warming up to 95 ℃ and add 21.7 parts of first section oxidation propylenes, reaction pressure 0.6MPa, reacted 2 hours, be warming up to 125 ℃ behind the slaking 1.5hr, after carrying out vacuum hydro-extraction, under this temperature, add 48.6 parts of second section oxidation propylenes, reacted 4 hours, after slaking analysis in 2 hours hydroxyl value is qualified, vacuumize and remove unreacted monomer and micromolecular compound, add phosphoric acid and Disodium pyrophosphate neutralizing agent, 124 ℃ of neutral temperatures, required time 1.5hr, slough the moisture content in the polyethers then, add 0.5 part of hexa-magnesium silicate absorption 0.5hr after, material is imported pressure filter, filtrate is the product polyether glycol in use fire resistant hard foam of polyurethane, its viscosity is 3200CP, and hydroxyl value (25 ℃) is 442mg KOH/g, moisture content (wt%) 0.05, PH6, molecular weight 450.
Embodiment two
Embodiment two and embodiment one are basic identical, and the difference sorbyl alcohol that is to feed intake is 11 parts, 8 parts of sucrose, 4 parts of glycerine, 0.2 part of potassium hydroxide solution, and concentration is 53%; First section reaction adds 22.7 parts of propylene oxides, 100 ℃ of temperature of reaction; Second section reaction adds 53.1 parts of propylene oxides, 128 ℃ of temperature of reaction; Reaction pressure is 0.4MPa.Product hydroxyl value 400mg KOH/g, viscosity 3800CP, moisture content 0.04, PH are 7.2, molecular weight 700.
Embodiment three
Embodiment three and embodiment one are basic identical, and the difference sorbyl alcohol that is to feed intake is 12.8 parts, 9 parts of sucrose, 6 parts of glycerine; First section reaction adds 21.3 parts of propylene oxides, 87 ℃ of temperature of reaction, reaction pressure 0.7MPa; Second section reaction adds 49.8 parts of propylene oxides, and 130 ℃ of temperature of reaction, reaction pressure are 0.5MPa.Product hydroxyl value 450mg KOH/g, viscosity 3000CP, moisture content 0.02, PH are 6.5, molecular weight 650.
Claims (9)
1, the preparation method of polyether glycol in use fire resistant hard foam of polyurethane, its feature comprises the following steps:
To be 24～31 parts initiator by weight, 0.1～0.5 part alkali hydroxide soln catalyzer, concentration is 30%～60%, joins in the reactor, vacuumizes deoxidation, fills nitrogen, opens stirring and is warming up to 80～100 ℃; The olefin oxide that accounts for total amount 30% is dropped in the still 80～100 ℃ of temperature of reaction, pressure 0.2～0.8MPa, 2～3 hours reaction times; Be warming up to 100～130 ℃, after the vacuum hydro-extraction, add remaining olefin oxide, reacted 4～7 hours; It is 68.5～75.9 parts that olefin oxide adds total amount twice; Adopt the mixture neutralizing agent solution neutralization of Disodium pyrophosphate and phosphoric acid, 120～130 ℃ of neutral temperatures, 1.5 hours time; Remove moisture in the reactant, add with the material gross weight than being 0.5% hexa-magnesium silicate adsorbents adsorb 0.5 hour, remove potassium, sodium ion; Elimination impurity promptly gets yellow thick product.
2, according to the preparation method of the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1, it is characterized in that described initiator comprises ethylene glycol, propylene glycol, glycerol, butyleneglycol, TriMethylolPropane(TMP), pentanediol, tetramethylolmethane, 1,2,6 ,-hexanetriol, sorbyl alcohol, Xylitol, N.F,USP MANNITOL, sucrose and methyl glucoside.
3,, it is characterized in that the catalyzer alkali metal hydroxide comprises potassium hydroxide and sodium hydroxide according to the preparation method of the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1.
4,, it is characterized in that the reactive polymeric pressure-controlling is at 0.4～0.6MPa according to the preparation method of the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1.
5, according to the preparation method of the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1, it is characterized in that polyreaction divides two sections to carry out, first section temperature of reaction is controlled at 85～95 ℃, and second section reaction is controlled at 110～125 ℃.
6,, it is characterized in that olefin oxide comprises propylene oxide, ethylene oxide according to the preparation method of the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1.
7, preparation method according to the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1, it is characterized in that in the autoclave that has whipping appts and inner coil refrigerating unit, drop into 13.7 parts of sorbyl alcohols, 9.7 parts of sucrose, 5.7 parts of glycerine, 0.23 part of potassium hydroxide solution, concentration is 48%, vacuumize deoxygenation, open stirring, heat up 95 ℃ and add 21.7 parts of first section oxidation propylenes, reaction pressure 0.6MPa, reacted 2 hours, heat up 125 ℃ behind the slaking 1.5hr and carry out vacuum hydro-extraction, the qualified back of moisture content adds 48.6 parts of second section oxidation propylenes under this temperature, reacted 4 hours, after slaking analysis in 2 hours hydroxyl value is qualified, vacuumize and remove unreacted monomer and micromolecular compound, add phosphoric acid and Disodium pyrophosphate neutralizing agent, 124 ℃ of temperature of reaction, required time 1.5hr, slough the moisture content in the polyethers then, after adding 0.5 part of hexa-magnesium silicate absorption 0.5hr material is passed through pressure filter, filtrate is product, makes polyether glycol in use fire resistant hard foam of polyurethane.
8, according to the preparation method of the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1, the sorbyl alcohol that it is characterized in that feeding intake is 11 parts, 8 parts of sucrose, 4 parts of glycerine, 0.2 part of potassium hydroxide solution, and concentration is 53%; First section reaction adds 22.7 parts of propylene oxides, 100 ℃ of temperature of reaction; Second section reaction adds 53.1 parts of propylene oxides, 128 ℃ of temperature of reaction; Reaction pressure is 0.4MPa.
9, according to the preparation method of the described polyether glycol in use fire resistant hard foam of polyurethane of claim 1, the sorbyl alcohol that it is characterized in that feeding intake is 12.8 parts, 9 parts of sucrose, 6 parts of glycerine; First section reaction adds 21.3 parts of propylene oxides, 87 ℃ of temperature of reaction, reaction pressure 0.7MPa; Second section reaction adds 49.8 parts of propylene oxides, and 130 ℃ of temperature of reaction, reaction pressure are 0.5MPa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200510045791 CN1290898C (en) | 2005-01-31 | 2005-01-31 | Method for preparing polyether glycol in use fire resistant hard foam of polyurethane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200510045791 CN1290898C (en) | 2005-01-31 | 2005-01-31 | Method for preparing polyether glycol in use fire resistant hard foam of polyurethane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1660918A CN1660918A (en) | 2005-08-31 |
| CN1290898C true CN1290898C (en) | 2006-12-20 |
Family
ID=35010494
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200510045791 Expired - Fee Related CN1290898C (en) | 2005-01-31 | 2005-01-31 | Method for preparing polyether glycol in use fire resistant hard foam of polyurethane |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1290898C (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102702505A (en) * | 2012-06-27 | 2012-10-03 | 淄博德信联邦化学工业有限公司 | High-temperature-resistant polyether polyol and preparation method thereof |
| CN104744683A (en) * | 2013-12-27 | 2015-07-01 | 上海东大化学有限公司 | Xylitol-initiated polyoxyethylene-polyoxypropylene ether copolymer and its preparation method and use |
| CN105111428A (en) * | 2015-08-31 | 2015-12-02 | 句容宁武新材料发展有限公司 | Preparation method of low-odor polyether polyol |
| CN105315452B (en) * | 2015-11-25 | 2017-09-22 | 山东一诺威新材料有限公司 | The preparation method of soluble polyurethane grouting material PPG |
| CN105820327B (en) * | 2016-05-24 | 2018-11-13 | 无锡市长安曙光手套厂 | High temperature resistant and corrosion resistant polyether polyol and preparation method thereof |
| CN105860051A (en) * | 2016-06-29 | 2016-08-17 | 句容宁武新材料股份有限公司 | Method for preparing low-odor polyether for polyurethane foam and application of prepared products |
| CN108203501B (en) * | 2016-12-02 | 2020-05-08 | 蓝星（北京）技术中心有限公司 | Preparation method of polyether polyol with high-efficiency catalytic activity |
| CN107840950A (en) * | 2017-11-28 | 2018-03-27 | 山东诺威新材料有限公司 | The production technology of rigid-foam polyether polyol |
| CN109206571A (en) * | 2018-08-24 | 2019-01-15 | 江苏斯瑞达新材料科技有限公司 | Washable slow rebound polyurethane foam and preparation method thereof |
| CN109306057B (en) * | 2018-09-29 | 2020-12-15 | 山东一诺威新材料有限公司 | Preparation method of polyether polyol special for OCF |
| CN109776748A (en) * | 2019-01-22 | 2019-05-21 | 天津爱德加科技有限公司 | A kind of full hydraulic matter polyurethane foam composition polyethers of high temperature resistant, hard polyurethane foams and preparation method thereof |
| CN115991866A (en) * | 2022-11-30 | 2023-04-21 | 惠州市红墙化学有限公司 | Preparation method of polyether for polyurethane semi-rigid foam |
-
2005
- 2005-01-31 CN CN 200510045791 patent/CN1290898C/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN1660918A (en) | 2005-08-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1290898C (en) | Method for preparing polyether glycol in use fire resistant hard foam of polyurethane | |
| CN101967226B (en) | Method for synthesizing high-activity high molecular weight polyether polyalcohol | |
| CN110885435B (en) | Process for preparing high functionality polyether polyols | |
| EP3249000B1 (en) | Method for circularly preparing polyether polyol by using dmc catalyst | |
| CN100390129C (en) | Bio-based polyhydric alcohol prepared by using rape seed oil | |
| CN104311813A (en) | Antioxidant polyether polyol and preparation method thereof | |
| CN101959931A (en) | Process for preparing polyols | |
| CN109306057B (en) | Preparation method of polyether polyol special for OCF | |
| CN102504891B (en) | Preparation method of glyceryl biological fuel additives | |
| CN102040732A (en) | Preparation method of polyether polyol cross-coupling agent | |
| CN111116894A (en) | Isosorbide-based polyether polyol, polyol composition and rigid polyurethane foam | |
| CN101967227A (en) | Synthetic method of slow resilience foam polyether polyol | |
| CN104497298A (en) | Method for preparing polyether polyol with low degree of unsaturation, high molecular weight and high activity | |
| CN103709392B (en) | The preparation method of polyether polyol for automobile sealant | |
| CN1293121C (en) | Polyether polyatomic alcohol preparation for subfluoride hard foamed material | |
| CN112724394B (en) | Preparation method of cellulose polyether polyol | |
| CN113980205B (en) | Process for preparing polymer polyols | |
| CN116253868A (en) | Preparation method of alcohol amine polyether polyol with high functionality | |
| CN101671253A (en) | Catalytic synthesis method of dimethyl carbonate | |
| CN112646164B (en) | Graphene composite bio-based polyether polyol and preparation method thereof | |
| JP2644327B2 (en) | Purification method of polyether polyol | |
| CN115572385B (en) | Preparation method of plant-based polyether polyol | |
| CN113667111A (en) | Preparation method of sorbitol-based high molecular weight polyether polyol | |
| CN105601902A (en) | Synthetic method of sucrose polyoxypropylene | |
| CN112724393B (en) | Preparation method of low-temperature sensitive high-temperature resistant polyether polyol |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20061220 Termination date: 20100131 |