CA1091684A - Low-temperature storage stable liquid diphenylmethane diisocyanates - Google Patents

Low-temperature storage stable liquid diphenylmethane diisocyanates

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Publication number
CA1091684A
CA1091684A CA298,313A CA298313A CA1091684A CA 1091684 A CA1091684 A CA 1091684A CA 298313 A CA298313 A CA 298313A CA 1091684 A CA1091684 A CA 1091684A
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Prior art keywords
isomer
percent
weight
liquid
compound
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CA298,313A
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French (fr)
Inventor
Helmut F. Reiff
Richard S. Pantone
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Bayer Corp
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Mobay Corp
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    • 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
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
    • C08G18/32Polyhydroxy compounds; Polyamines; Hydroxyamines
    • C08G18/3203Polyhydroxy compounds
    • C08G18/3206Polyhydroxy compounds aliphatic
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C263/00Preparation of derivatives of isocyanic acid
    • C07C263/18Separation; Purification; Stabilisation; Use of additives
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C265/00Derivatives of isocyanic acid
    • C07C265/14Derivatives of isocyanic acid containing at least two isocyanate groups bound to the same carbon skeleton
    • 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
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/4833Polyethers containing oxyethylene units
    • 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
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/74Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
    • 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
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/74Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/76Polyisocyanates or polyisothiocyanates cyclic aromatic
    • C08G18/7657Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings
    • C08G18/7664Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups
    • C08G18/7671Polyisocyanates or polyisothiocyanates cyclic aromatic containing two or more aromatic rings containing alkylene polyphenyl groups containing only one alkylene bisphenyl group

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

LOW-TEMPERATURE STORAGE STABLE
LIQUID DIPHENYLMETHANE DIISOCYANATES

ABSTRACT OF THE DISCLOSURE
The instant invention is directed to novel low temperature, storage stable liquid diphenylmethane diisocyanates and to the method of their preparation. The diisocyanates of the instant invention are produced by reacting diphenylmethane diisocyanates having a specified 2,4'-isomer content with polyoxyethylene glycols having molecular weights of from 150 to 1500. It has been surprisingly found that the products of the instant invention are both stable and liquid at -5°C for at least 48 hours. In fact, in many instances, the products of the instant invention show no tendency to crystallize even when stored at -22°C for 100 hours.

Description

Mo-1706 LOW-TEMPERATURE STORAGE STABLE
LIQUID DIPHENYLMETHANE DIISOCYANATES

BACKGROUND OF THE INVENTION
It is well known that diisocyanates which are liquid at room temperature (i.e., about 25C) have numerous advantages over solid diisocyanates because they are easier to mix and work with. However, diisocyanates which are liquid at room temperature and which are used on a large technical scale, such as toluene diisocyanate or hexamethylene diisocyanate, are as a rule physiologically harmful due to their high vapor pressure and therefore can only be used if certain safety precautions are taken. For this reason, various attempts have been made, either to start with diisocyanates that are normally liquid at room temperature and to reduce their physiological effects by certain procedures or to start with diisocyanates that are solid at room temperature and to convert these into liquid form. In both cases, however, one usually obtains either isocyanates of higher valency, i.e., tri- or polyisocyanates or higher molecular weight diisocyanates or a combination of these effects.

The most important diisocyanates which are solid at room temperature and which are readily available on a large commercial scale are 4,4'-diphenylmethane diisocyanate and the 2,4'-isomer thereof which melt at 39C and 34.5C
respectively. Attempts have already been made to liquify both the 4,4'-diphenylmethane diisocyanate and a mixture of the 4,4'-diphenylmethane diisocyanate and a small amount of the 2,4'-isomer. Thus, for example, in U. S. Patent 3,644,457, 1 mol of a diphenylmethane diisocyanate is reacted with from about 0.1 to about 0.3 mols of poly-1,2-'r~
Mo-1706 ~

propylene ether ~lycol. Whlle the products made accor~ing to this patent have met with commercial success, they still suffer from a serious drawback. Specifically, it has been found that these adducts generally will crystallize 5 anywhere from 5C to as high as 25C. In fact, when supplied in commercial quantities, these adducts are generally transported in heated trucks. Additionally, in order to thaw the materials it is generally necessary to heat them to somewhere in excess of 50 to 60C. While in warmer climates, there may not be any problem, in colder areas where the product may be stored in tanks over a period of time, this tendency to crystallize can become a very serious problem. Similar attempts to form liquid diphenylmethane diisocyanates have been described for example, in U.S. Patents 3,384,653 and 3,394,164.
The attempts to liquify in both of these instances were based on the addition of, in one case, a trihydrocarbyl phosphate, and, in the other case, small amounts of phosphoric acid. In any event, the storage stability of both of these types of products is again quite good around room temperature, but as the temperature decreases, both types of materials tend to crystallize.
In U.S. Patent 4,118,411, issued October 3, 1978, diisocyanates are described which are both stable and liquid at -5C for at least 4g hours. The diisocyanates disclosed therein are produced by reacting a diphenyl-methane containing at least 15 percent by weight of the
2,4'-isomer with a propylene glycol or poly-1,2-propylene ether glycol. Although such products represent an important advance in the art, the search has continued for other liquid organic diisocyanates.
Mo-1706 -2-:~139~ 4 It is therefore an object of this invention -to provide improved liquid organic diisocyanates which are liquid and stable at temperatures lower than room tempera-ture. A further object of this invention is to provide organic diisocyanates which remain liquid even on prolonged storage at low temperatures.

DESCRIPT ON OF THE INVENTIO
The instant invention is therefore directed to novel diisocyanate compounds which are both stable and liquid at -5C for at least 48 hours which diisocyanate compound comprises the reaction product of a diphenyl-methane diisocyanate containing at least 20% by weight of the 2,4'-isomer with polyoxyethylene glycol having a molecular weight of from 150 to 1500. The materials are reacted in an NCO/OH ratio of from about 3 : 1 to about 15 : 1, preferably from about 3 : 1 to about 10 : 1 and most preferably from about 3 : 1 to about 6 : 1. It has also been found that many of the novel diisocyanate compounds herein are both stable and liquid at -22C for 100 hours.

The glycol and the isocyanate can be reacted at temperatures ranging anywhere from room temperature (i.e., about 25) up to 125C. Preferably, the reaction tempera-ture is from room temperature to about 90C and most preferably, from about 40C to about 80C.

In general, the diphenylmethane diisocyanates usable according to the instant invention must contain at least 20 percent by weight of the 2,4'-isomer. While theoretically, there is no upper limit to the amount of 2,4'-isomer which could be present in the isocyanate, Mo-1706 -3-~t31t;~

as a practical ma-tter, due to availability in the present day isocyana-te market, it is generally not possible to have the 2,4'-isomer content in e~cess of 70 percent. Thus, as a practical rule, the diphenylmethane diisocyanates used according to the instant invention will contain from about 20 to about 70 percent by weight of the 2,4'-isomer with the balance being the 4,~'-isomer and 2,2'-isomer and/or various MDI dimers (the 2,2'-isomer and any dimer are generally present only in trace amounts, i.e., less than 1 percent by weight). The lower limit of 20 percent by weight of the 2,4'-isomer is in fact somewhat marginal. In fact, it has been found that at the 20 percent level, some of the reaction products formed are low temperature storage stable while others are not. Preferably, the 2,4'-isomer content is from about 25 to about 65 percent by weight and most preferably from about 40 to about 65 percent by weight.

The liquid diisocyanates which can be prepared according to the instant invention have a relatively low viscosity and can therefore be worked up very easily, e.g., they can be cast or metered through pumps. In addition, they have a very low vapor pressure and are therefore substantially physiologically harmless. Since the reaction can generally be carried out at relatively low temperatures, the diisocyanate structure of the product of the process is completely preserved. Allophanate formation by the reaction of the resulting urethane groups with the iso-cyanate group to produce a polyisocyana-te apparently does not take place to any large degree. This is true even when forming the reaction product at a temperature of 125C.

Mo-1706 -4-31~

The polyoxyethylene glycols usable in the instant invention include essentially any ranging from a rnolecular weight of 150 (i.e. triethylene glycol) up to molecular weights of about 1500. Specific examples include tri-ethylene glycol, tetraethylene glycols, and various poly-oxyethylene glycols.

The process of the instant invention may be carried out by introducing the glycols into the diisocyanate at temperatures of from room temperature up to about 125C with stirring. Alternatively, the diisocyanate can be introduced into the glycols. The isocyanate content of the products of the process generally amounts to from as low as about 10 percent to as high as about 30 percent.

The products of the process can be used for all types of different polyaddition reactions in the lacquer and plastics industries, e.g. for the production of polyurethane foams or polyurethane elastomers which are in turn useful for the preparation of cushions or gear wheels respectively. Because of their low freezing point, the materials can be transported and stored at reasonably cold temperatures. In fact, it will be clear from the examples which follow, many of the products of the instant invention do not freeze when stored at -22C
for 100 hours. Yet a further advantage of the reaction products of the instant invention resides in the fact that even if the products should freeze, -they will readily thaw at room temperature. This is completely different from the materials disclosed in U.S. Patent 3,644,457, which upon freezing, must be heated to in excess of 50C.

Mo-1706 -5-
3~~

The invention i9 further illustrated by the following examples in which all parts are by weight unless otherwise specified.

Mo-1706 -6-3 iL~if.~'1 EXAMPLES

In these eight examples, a diphenylmethane diisocyanate ~containing 35 percent by weight of the
4,4l-isomer and 65 percent by weight of the 2,4'-isomer) and the various glycols specified in TABLE I were combined under vigorous stirring at 25C. After a few minutes, the reaction mixtures turned clear and slight exotherm of up to about 50 to 60C was observed. After the exotherm had leveled o~f, stirring was continued for an additional
5 hours. Samples were then analyzed for viscosity and NCO
content and then stored in a freezer for 48 hours at -5C.
After the 48 hours storage, the samples were removed from the freezer. Results are set forth in TABLE I. The amounts of glycols and isocyanates added were such that the NCO/OH ratio was as specified in the table. Examples 1 and 2 represent comparative examples.

Mo-1706 -7-~V.~3~

~, o r-l ~ ~ aJ
a) ,~ ~
~r~l U~ a~ ~a rd r~ rC~ ~ rd h ,Q ~~ rl (L) O (~ O~3 ~ ~) t~lti1tJ~ t~ t~ tT' ~ ~) ~O O --Irl rl rl ~1 rl U~ U~U U~ ~Ir-l ~I r~
, ~) o rc~ o r~ -rl U
tO Q
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~1 ~ ,S: ~1 o a.~ o o u~ U~
u ~ ~ d co ~ ~ o ~ u~
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r~ ~ I~ ) O
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I ~r ~ ~ ~ o ~J O ~ ~ N ~J
rC
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uIsl 1~ ~ a~
\ ~ r-l In ~ ~ ~ ~ o m u E~

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0 ,1 ~ o o O ~ ~ ~r ~r ~ ~r ~ oo co . O
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r-l U ~~ ~ ~ ~ ~
O ~ o ~ o ~J ~ ~a~ ~ o~ o o r ~ O ~r~l a) 3 a) ~]) ~1) ~ a~ aJ ~ s ~1 ~ ~
u >~ h ~1 ~ ~I r-l 11) 1~1 a) r-l ~1) r-l O
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Zr-l t~l '7~r 11~) ~D 1~ CO

~lo- 1 7 0 6 - 8--l!~D~it;1~4 Af-ter bringing the products of Examples 3 through 8 back to room temperature, viscosi-ties and ~ NCO were rechecked and found to be unchanged.

The process of Examples l through 8 were followed except that the isomer distribution was varied as set forth in TABLE II. A constant NCO/OH ratio of 4.95 was used in each instance. The glycol used in each example was tetra-ethylene glycol. Results are set forth in TABLE II. After bringing the products of Examples ll through 13 back to room temperature, viscosities and % NCO were rechecked and found to be unchanged.

Mo-1706 -9-J~

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Mo-1706 -10-~3~

EXAMæLES 14 T~IROUG~I 17 The process of Examples 1 throuyh 8 was followed using diphenylmethane diisocyanate containiny 65 percent by weight of the 2,4'-isomer and a polyethylene glycol having an average molecular weight o~ 600. The reaction temperature was 25C and exotherms were found to be between 35C and 50C. After the exotherm had leveled off, stirring was continued for 5 hours. Various NCO/OH ratios were used as specified ln TABLE III. Results are set forth in TABLE
III. After bringing the products back to room temperature, viscosities and % NCO were rechecked and found to be unchanged.

TABLE III

Example NCO/OH ~ NCO by weight Viscosity Storage No. Ratio calc. found cps, 25C Stability 48 hrs. @-5C

14 10 24.4 24.0115 liquid 8 22.6 22.2266 liquid 16 4.9 17.9 17.21660 liquid 17 3.0 12.4 11.77130 liquid The process of Examples 1 through 8 was followed using an NCO/OH ratio of 3.72, a diphenylmethane diisocyan-ate containing 65% by weight of the 2,4'-isomer, and tri-ethylene glycol, but using various reaction temperatures,and heated for the times specified in TABLE IV. The temperature, times of reaction and results were as set forth in TABLE IV. ~ NCO and viscosities remained Mo-1706 -11-3~

unchanged after -the products were brought back to room temperature.

TABLE IV

Reaction + Storage Example Reaction Time ~ NCO Viscosity Stability No. Temperature in hours Found cps, 25C 48 hours @ -5C

18ambient 8 hrs. 21.2 4000 liquid 19 40C 8 hrs. 21.1 4300 liquid 65C 3 hrs. 21.1 4200 liquid 21 105C 1 hr. 20.7 4425 liquid + All viscosities are measured the day materials were prepared. It was observed that these materials have a thixotropic character.

The products of Examples 2 through 21 were all stored in a deep-freezer for 100 hours at -22C and checked for stability against freezing and/or crystallization. The results were as set forth in TABLE V.

Mo-1706 -12-~L~93~F.3'~

TABLE V

Example 100 hrs./-22C Comments No Storaae StabilitY
.~ .

2 gel very high viscosity, gel-like material 3 liquid none 4 liquid liquid "
6 liquid "
7 complete material melted to a perfect solid liquid at ambient temperature ~ without heating, shaking or J stirring.
8 .,
9 complete materials do not melt at solid ambient temperature; they ) remain a white crystalline J solid.
10 '
11 liquid none
12 ~
13 " "
14 ~
" "
16 " ~
17 " "
18 " "
19 ~
" "
21 "

Mo-1706 -13-3~

To 300 grams of diphenylmethane diisocyanate with a 2,4'-isomer content of 20 percent were added 240 grams of polyethylene glycol (molecular weight of 600) at 50C under stirring. The temperature of the reaction mixture increased to about 85C and then dropped within one hour to about 55C. Stirring was continued for three hours at 55C. The NCO/OH ratio used was 3. The percent NCO in the product was found to be 11.8 percent while the viscosity at 25C was found to be 15,400 cps. The product remained in the liquid state when stored at -5C for 48 hours and when stored at -22C for 100 hours. After storage stability was established, no change in either NCO
content or viscosity could be determined.

This example serves to illustrate that, as noted earlier, at the 20 percent 2,4'-isomer content level it is certainly possible to produce liquid products within the defined invention (compare Example 10).

The process of Examples 1 through 8 was followed using an NCO/OH ratio of 4.g5, a diphenylmethane diisocyan-ate containing 65 percent by weight of the 2,4'-isomer and triethylene glycol, but using various reaction temperatures and heated for the times specified in TABLE VI. The temper-atures, times of reaction and results were as set forth inTABLE VI. Percent NCO and viscosities remained unchanged after the products were brought back to room temperature.

Mo-1706 -14-~lf~

TABLE VI

Reaction Storage Example Reac-tion Time ~ NCO Viscosity Stability No. Temperature in hours Found cps, 25C 48 hours @ -5C

23 25C 19 hrs. 23.9 570 liquid 24 40C 5 hrs. 23.9 570 liquid 65C 4 hrs. 24.2 550 liquid 26 105C 1 hr. 23.8 605 liquid When stored for 100 hours at -22C, the products of Examples 23 through 26 remained liquid.

It is to be understood that the foregoing examples are given for the purpose of illustration and that various other materials within the definition of the claims could be used. Although the invention has been described in detail for the purpose of illustration, it is to be understood that such detail is solely for that purpose and that variations can be made therein by those skilled in the art without departing from the spirit and scope of the invention except as it may be limited by the claims.

Mo-1706 -15-

Claims (18)

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:-
1. A diisocyanate compound which is both s-table and liquid at -5°C for at least 48 hours, comprising the reaction product of:

(a) a diphenylmethane diisocyanate contain-ing at least 20 percent by weight of the 2,4'-isomer, and (b) a polyoxyethylene glycol having a molecular weight of from 150 to 1500.
2. The compound of Claim 1 wherein said diphenyl-methane diisocyanate comprises (a) from about 20 to about 70 percent by weight of the 2,4'-isomer, and the balance being (b) the 4,4'-isomer.
3. The compound of Claim 2, wherein said diphenyl-methane diisocyanate comprises:

(a) from about 25 to about 65 percent by weight of the 2,4'-isomer, and the balance being (b) the 4,4'-isomer.
4. The compound of Claim 3, wherein said diphenyl-methane diisocyanate comprises:

(a) from about 40 to about 65 percent by weight of the 2,4'-isomer, and the balance being (b) the 4,4'-isomer.
5. The compound of Claim 2, wherein components (a) and (b) are used in such quantities that the NCO/OH
ratio is from about 3 : 1 to about 15:1.
6. The compound of Claim 5, wherein said ratio is from about 3:1 to about 10:1.
7. The compound of Claim 6, wherein said ratio is from about 3:1 to about 6:1.
8. The compound of Claim 1, wherein components (a) and (b) are used in such quantities that the NCO/OH ratio is from about 3:1 to about 15:1.
9. The compound of Claim 8, wherein said ratio is from about 3:1 to about 10:1.
10. The compound of Claim 9, wherein said diphenylmethane diisocyanate comprises:

(a) from about 25 to about 65 percent by weight of the 2,4'-isomer, and the balance being (b) the 4,4'-isomer.
11. The compound of Claim 9, wherein said ratio is from about 3:1 to about 6:1.
12. The compound of Claim 11, wherein said diphenylmethane diisocyanate comprises:

(a) from about 40 to about 65 percent by weight of the 2,4'-isomer, and the balance being (b) the 2,4'-isomer.
13. A process for the production of diisocyanate compounds which are both stable and liquid at -5°C for at least 48 hours which comprises reacting:
(a) a diphenylmethane diisocyanate contain-ing at least 20 percent by weight of the 2,4'-isomer, and (b) a polyoxyethylene glycol having a molecular weight of from 150 to 1500.
14. The process of Claim 13, wherein said components (a) and (b) are reacted at a temperature of from room temperature to about 125°C.
15. The process of Claim 14, wherein said diphenylmethane diisocyanate comprises (a) from about 20 to about 70 percent by weight of the 2,4'-isomer, and the balance being (b) the 4,4'-isomer.
16. The process of Claim 15, wherein components (a) and (b) are used in such quantities that the NCO/OH

ratio is from about 3:1 to about 15:1.
17. The process of Claim 16, wherein said components (a) and (b) are reacted at a temperature of from room tempera-ture to about 90°C.
18. The process of Claim 17, wherein said components (a) and (b) are reacted at a temperature of from about 40°C to about 80°C.
CA298,313A 1977-03-18 1978-03-02 Low-temperature storage stable liquid diphenylmethane diisocyanates Expired CA1091684A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US05/778,896 US4115429A (en) 1977-03-18 1977-03-18 Low-temperature storage stable liquid diphenylmethane diisocyanates
US778,896 1985-09-23

Publications (1)

Publication Number Publication Date
CA1091684A true CA1091684A (en) 1980-12-16

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Country Link
US (1) US4115429A (en)
JP (1) JPS53116358A (en)
BE (1) BE864962A (en)
CA (1) CA1091684A (en)
DE (1) DE2810596A1 (en)
FR (1) FR2383977A1 (en)
GB (1) GB1577999A (en)
IT (1) IT1104612B (en)
NL (1) NL7802832A (en)

Families Citing this family (70)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4234714A (en) * 1979-03-29 1980-11-18 Textron Inc. Preparation of single-phase, urethane prepolymers from hydroxy-terminated diene polymers
DE3042821A1 (en) * 1980-11-13 1982-06-09 Bayer Ag, 5090 Leverkusen METHOD FOR SEALING CONSTRUCTIONS
JPS57109756A (en) * 1980-12-26 1982-07-08 Mitui Toatsu Chem Inc Isocyanate composition
EP0057862A1 (en) * 1981-02-05 1982-08-18 Mobay Chemical Corporation Partially carbodiimidised methylene bis (phenylisocyanate) having low temperature storage stability, a process for its preparation and its application as a starting material for the diisocyanate-polyaddition reaction
US4321333A (en) * 1981-04-16 1982-03-23 The Upjohn Company Polyurethane prepared from polyisocyanate blend
US4480070A (en) * 1982-05-28 1984-10-30 The Upjohn Company Compositions and process
DE3241450A1 (en) * 1982-11-10 1984-05-10 Basf Ag, 6700 Ludwigshafen DIPHENYLMETHANE-DIISOCYANATE-BASED POLYISOCYANATE MIXTURES CONTAINING LIQUID URETHANE GROUPS, METHOD FOR THE PRODUCTION THEREOF AND THE USE THEREOF FOR THE PRODUCTION OF POLYURETHANE SOFT FOAMS
JPS60501660A (en) * 1983-06-27 1985-10-03 ホステツトラ−,フリツツ Cold storage stable mixtures of prepolymers and flow modifiers
US4800040A (en) * 1983-06-27 1989-01-24 Fritz Hostettler Low temperature, storage stable mixtures of prepolymers and flow modifiers
US4490300A (en) * 1983-09-30 1984-12-25 Mobay Chemical Corporation Liquid diphenylmethane diisocyanate compositions
US4490301A (en) * 1983-09-30 1984-12-25 Mobay Chemical Corporation Liquid diphenylmethane diisocyanate compositions
US4490302A (en) * 1983-11-25 1984-12-25 Mobay Chemical Corporation Liquid diphenylmethane diisocyanate compositions
DE3401166A1 (en) * 1984-01-14 1985-07-18 Bayer Ag, 5090 Leverkusen METHOD FOR PRODUCING URETHANE-MODIFIED POLYISOCYANATE PREPARATIONS AND THEIR USE IN THE PRODUCTION OF POLYURETHANE PLASTICS
DE3405939A1 (en) * 1984-02-18 1985-08-22 Bayer Ag, 5090 Leverkusen METHOD FOR PRODUCING URETHANE-MODIFIED POLYISOCYANATE PREPARATIONS AND THEIR USE IN THE PRODUCTION OF POLYURETHANE PLASTICS OR POLYISOCYANURATE PLASTICS
US4535110A (en) * 1984-06-25 1985-08-13 The Budd Company Dual functional additive
US4539157A (en) * 1984-12-14 1985-09-03 Mobay Chemical Corporation Liquid diphenylmethane diisocyanate compositions
US4539158A (en) * 1984-12-14 1985-09-03 Mobay Chemical Corporation Liquid diphenylmethane diisocyanate compositions
US4539156A (en) * 1984-12-14 1985-09-03 Mobay Chemical Corporation Liquid diphenylmethane diisocyanate compositions
DE3526233A1 (en) * 1985-07-23 1987-01-29 Bayer Ag METHOD FOR THE PRODUCTION OF POLYISOCYANATE PREPARATIONS HAVING UREA AND / OR BIURET GROUPS, THE POLYISOCYANATE PREPARATIONS AVAILABLE ACCORDING TO THIS METHOD AND THE USE THEREOF AS ISOCYANATE COMPONENT ADHESIVE FOR THE ADMINISTRATION OF ISOCYANATE COMPONENT
DE3527531A1 (en) * 1985-08-01 1987-02-12 Bayer Ag METHOD FOR PRODUCING URETHANE-MODIFIED POLYISOCYANATE PREPARATIONS, THE POLYISOCYANATE PREPARATIONS OBTAINED BY THIS METHOD AND THEIR USE IN THE PRODUCTION OF PLASTICS BASED ON POLYISOCYANATE
US4797226A (en) * 1985-09-24 1989-01-10 Fritz Hostettler Low temperature, compatible mixtures of polyether prepolymers and flow modifiers
US4910333A (en) * 1987-06-03 1990-03-20 Mobay Corporation Liquid diphenylmethane diisocyanate compositions
US4767796A (en) * 1987-12-17 1988-08-30 The Dow Chemical Company Hard segment containing prepolymers from cycloalkane diols
US4883909A (en) * 1988-05-11 1989-11-28 Mobay Corporation Liquid diphenylmetane diisocyanate compositions
US5298303A (en) * 1989-03-20 1994-03-29 Reeves Brothers, Inc. Fabric structure for severe use applications
US5096992A (en) * 1989-03-20 1992-03-17 Reeves Brothers, Inc. Use of modified diisocyanates for preparing linear thermoplastic polyurethane elastomers having improved properties
US5001208A (en) * 1989-03-20 1991-03-19 Reeves Brothers, Inc. Linear polyurethane elastomer compositions based on mixed polycarbonate and polyether polyols
US5013811A (en) * 1989-03-20 1991-05-07 Reeves Brothers, Inc. Use of modified diisocyanates for preparing linear thermoplastic polyurethane elastomers having improved properties
US5130384A (en) * 1989-03-20 1992-07-14 Reeves Brothers, Inc. Calenderable thermoplastic polyurethane elastomer compositions containing millable linear polyurethanes
US5264620A (en) * 1989-12-06 1993-11-23 Basf Corporation Prepolymer compositions derived from liquid methylene bis (phenylisocyanate) and polytetramethylene ether glycol
CA2029504C (en) * 1989-12-06 1995-06-06 Thirumurti Narayan Prepolymer compositions derived from liquid methylene bis(phenylisocyanate) and polytetramethylene ether glycol
US5110666A (en) * 1991-05-06 1992-05-05 Reeves Brothers, Inc. Coated fabric structure for air bag applications
JPH0525006U (en) * 1991-06-04 1993-04-02 新キヤタピラー三菱株式会社 Return circuit filter base structure
US5621016A (en) * 1992-04-16 1997-04-15 Imperial Chemical Industries Plc Polyisocyanate compositions and low density flexible polyurethane foams produced therewith
US5288899A (en) * 1993-06-30 1994-02-22 Miles Inc. Liquification of diphenylmethane diisocyanate by partially reacting the isocyanate groups with blocking agents
US5319054A (en) * 1993-09-02 1994-06-07 Miles Inc. Liquid methylene diphenyl diisocyanate
US5440003A (en) * 1993-09-02 1995-08-08 Miles Inc. Liquid methylene diphenyl diisocyanate
US5319053A (en) * 1993-09-02 1994-06-07 Miles Inc. Liquid diphenylmethane diisocyanate
US5350778A (en) * 1993-10-28 1994-09-27 Miles Inc. Polyisocyanate based upon 4,4'- and 2,4'-diphenylmethane diisocyanates and use thereof in a rim process
CA2117740A1 (en) * 1993-10-28 1995-04-29 Michael F. Hurley Polyisocyanate based upon 4,4'-and 2,4'-diphenylmethane diisocyanates and use thereof in a rim process
CA2117741A1 (en) * 1993-10-28 1995-04-29 Michael F. Hurley Rim process utilizing isocyanates based upon 2,4'-and 4,4'- diphenylmethane diisocyanate
US5567793A (en) * 1995-06-06 1996-10-22 Bayer Corporation Urethane-free, diphenylmethane diisocyanate prepolymers and process for their production
US5686042A (en) * 1995-06-07 1997-11-11 Bayer Corporation Rim process using liquid methylene diphenyl diisocyanate
US5663272A (en) * 1995-12-22 1997-09-02 Bayer Corporation Allophanate-modified diphenylmethane diisocyanates and processes for their production and use
US5679756A (en) * 1995-12-22 1997-10-21 Optima Inc. Optical thermoplastic thiourethane-urethane copolymers
US5889068A (en) * 1997-07-24 1999-03-30 Bayer Corporation Water blown polyurethane soling systems
US6197878B1 (en) 1997-08-28 2001-03-06 Eastman Chemical Company Diol latex compositions and modified condensation polymers
WO2000052083A1 (en) 1999-03-03 2000-09-08 Eastman Chemical Company Silicone polymer diol compositions and condensation polymer/silicone polymer blends
BR0008669A (en) 1999-03-03 2002-02-05 Eastman Chem Co Process for the production of a mixture of a first polymer / polymer of the amide type, product, and, mixture of a first polymer / polymer of the amide type
JP2003503518A (en) 1999-06-18 2003-01-28 イーストマン ケミカル カンパニー Amide-type polymer / silicone polymer blend and method for producing the same
BR0011676A (en) 1999-06-18 2002-03-12 Eastman Chem Co Method of producing a mixture of nylon 6 / silicone polymer, product, mixture of nylon 6 / silicone polymer, and method of producing a mixture of polymer type amide / silicone polymer product
US6462109B1 (en) 1999-10-12 2002-10-08 Eastman Chemical Company Surfactantless latex compositions and methods of making polymer blends using these compositions
US6277943B1 (en) 1999-12-10 2001-08-21 Bayer Corporation One-shot polyurethane elastomers with very low compression set
US6248856B1 (en) 1999-12-10 2001-06-19 Bayer Corporation One-shot polyurethane elastomers with very low compression sets
US6482913B1 (en) 2000-02-07 2002-11-19 Bayer Aktiengesellschaft Liquid MDI adducts wtih improved freeze stability
US6376567B1 (en) 2000-12-07 2002-04-23 Bayer Corporation Polyisocyanate compositions and a process for the production of low-density flexible foams with low humid aged compression sets from these polyisocyanate compositions
US6844390B2 (en) * 2001-04-09 2005-01-18 Eastman Chemical Company Modified alkyd compositions comprising polyol latex compositions and processes of making them
US6699931B2 (en) 2001-04-09 2004-03-02 Eastman Chemical Company Modified alkyd compositions comprising diol latex compositions and processes of making the same
US20090005476A1 (en) * 2001-04-09 2009-01-01 Eastman Chemical Company Polyol latex compositions and process of making them
US7790907B2 (en) * 2006-07-21 2010-09-07 Basf Corporation Method of producing a uretonimine-modified isocyanate composition
US20080085987A1 (en) * 2006-10-05 2008-04-10 Thomas Savino Method of producing a uretonimine-modified isocyanate composition
WO2008057886A2 (en) * 2006-11-01 2008-05-15 Dow Global Technologies Inc. Polyurethane compositions and articles prepared therefrom, and methods for making the same
US8110704B2 (en) * 2006-11-02 2012-02-07 Bayer Materialscience Llc Process for the production of stable polymers
BRPI0719500B1 (en) 2006-12-21 2023-10-10 Dow Global Technologies Inc PROCESS FOR PREPARING A FUNCTIONALIZED MULTIBLOCK OLEFIN INTERPOLYMER AND PROCESS FOR PREPARING AN IMIDE FUNCTIONALIZED MULTIBLOCK INTERPOLYMER
DE102007044034A1 (en) * 2007-09-14 2009-03-19 Bayer Materialscience Ag polyisocyanate
US20090156777A1 (en) 2007-12-17 2009-06-18 Nodelman Neil H Freeze-stable aromatic diisocyanates and processes for the preparation of these freeze-stable products
KR20120050412A (en) 2009-06-18 2012-05-18 다우 글로벌 테크놀로지스 엘엘씨 Color-stable, halogen-free flame retardant compositions
WO2011003529A1 (en) * 2009-07-07 2011-01-13 Bayer Materialscience Ag Polyurethanes and use thereof
BR112012011124A2 (en) * 2009-11-12 2016-07-05 Kraton Polymers Us Llc block copolymer composition
US20230106532A1 (en) 2020-04-07 2023-04-06 Covestro Deutschland Ag Cold-stable nco prepolymers, method for the preparation and use thereof

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3362979A (en) * 1964-01-02 1968-01-09 Jefferson Chem Co Inc Mixtures of methylene-bridged polyphenyl polyisocyanates
US3394165A (en) * 1965-10-24 1968-07-23 Upjohn Co Stabilized methylenebis-(phenyl isocyanate) compositions
DE1618380C3 (en) * 1967-03-08 1975-09-11 Bayer Ag, 5090 Leverkusen Process for the production of a diphenylmethane diisocyanate preparation which is liquid at room temperature
GB1377676A (en) * 1972-09-21 1974-12-18 Ici Ltd Isocyanate compositions
NL178871C (en) * 1972-09-26 Ici Ltd PROCESS FOR PREPARING A LIQUID DIPHENYLMETHANE DIISOCYANATE PRODUCT AND FOR PREPARING OR MANUFACTURING A POLYURETHANE USING SUCH ISOCYANATE PRODUCT.
US4055548A (en) * 1976-09-17 1977-10-25 The Upjohn Company Storage-stable liquid polyisocyanate composition

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NL7802832A (en) 1978-09-20
IT7848451A0 (en) 1978-03-16
IT1104612B (en) 1985-10-21
FR2383977A1 (en) 1978-10-13
BE864962A (en) 1978-09-18

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