CA1053652A - Stable, pumpable, aqueous suspensions of organic peroxides - Google Patents

Stable, pumpable, aqueous suspensions of organic peroxides

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Publication number
CA1053652A
CA1053652A CA246,992A CA246992A CA1053652A CA 1053652 A CA1053652 A CA 1053652A CA 246992 A CA246992 A CA 246992A CA 1053652 A CA1053652 A CA 1053652A
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Canada
Prior art keywords
hlb
composition
polyethylene oxide
value
emulsifier
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
Application number
CA246,992A
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French (fr)
Inventor
Hendrik H. J. Oosterwijk
Reinder Torenbeek
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Akzona Inc
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Akzona Inc
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Priority claimed from NL7503051A external-priority patent/NL186816C/en
Priority claimed from NL7507859A external-priority patent/NL179375C/en
Application filed by Akzona Inc filed Critical Akzona Inc
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Publication of CA1053652A publication Critical patent/CA1053652A/en
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/28Oxygen or compounds releasing free oxygen
    • C08F4/32Organic compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F2/00Processes of polymerisation
    • C08F2/12Polymerisation in non-solvents
    • C08F2/16Aqueous medium
    • C08F2/18Suspension polymerisation

Abstract

ABSTRACT OF THE DISCLOSURE

Stable, pumpable, highly concentrated aqueous suspensions of organic peroxides containing (a) nonionic emulsifiers having a maximum HLB-value of 12.5 and (b) nonionic emulsifiers having a minimum HLB-value of 12.5 or anionic emulsifiers. These suspensions are particularly suitable for the (dis) continuous polymerization of vinyl chloride. There is far less reactor fouling than when in a polymerization under the same conditions use is made only of a solid peroxydicarbonate. The suspensions can also be used in the polymerization of acrylates and the copolymerization of styrene.

Description

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BACKGROUND OF THE INVENTION
The invention relates to a non-segregating, pumpable organic peroxide-containing aqueous suspension suitable for the (co)polymerization of ethylenically unsaturated monomers and to this suspension per se It is known that vinyl halides such as vinyl chloride;
vinyl bromide; and vinyl fluoride can be polymerized or, in combination with vinalidene halides such as vinylidene chloride and vinylidene fluoride or in combination with other terminal 10 C~2 = C = groups containing compounds, such as ethylene, pro-pylene and vinyl acetate, can be copolymerized. This poly-~; merization or copolymerlzation usually takes place in water. -To this end, the monomer to be polymerized or the monomer -mixture to be copolymerized is dispersed in water in the pre-sence of a protective colloid or an emulsifier, followed by the addition o~ a compound yielding free radicals to initiate (co)polymerization. For this purpose, use may be made of at room temperature sclid peroxydicarbonates such as dimyristyl peroxydicarbonate, dicetyl peroxydicarbonate, distearyl 20 peroxydicarbonate, bis (4-tert. butylcyclohexyl) peroxydicar-~ bonate, bi~ (4-tert, amylcyclohexyl) peroxydicarbonate, di-.3 cyclohexyl peroxydicarbonate and dibenzyl peroxydicarbonate.
Said peroxides display storage stability at room temperature.
j When for feeding purposes, however, these peroxy 3 dicarbonates are dissolved in organic solvents such as acetone, benzene or chloroform, the chemical stability of these peroxy compounds very much decreases. Moreover, such æolutions may give rise to strong reactions, spontaneous ignition and even explosions if no care is taken that the heat released upon de-30 composition is carried off.
U S patent Specification 3,825,509 describes a process for the suspension polymerization of vinyl chloride .~ ~

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alone or in combination with vinylidene monomers copolymerizable therewith, in which process the initiator is an emulsion of an organic peroxide in an aqueous solution containing 1 - 10% by weight of polyvinyl alcohol and 1 - 6% by weight of polyoxy-ethylene sorbitan monolaurate.
This emulsion has the disadvantage that it must not contain more than about 19% by weight of organic peroxide, higher concentration leading to a too viscous emulsion which is, therefore, difficult to handle. The additional disadvantage to these emulsions is that it can only be prepared at tempera-tures in the range of 5 - 10C and must be stored at 0C or even lower temperature.
U.S Patent Specification 3,507,800 describes a flame resistant, pasty composition which mainly consists of water, an organic peroxide and a mutual solvent for the water and the organic peroxide. In the patent specification, a distinction is made between on the one hand peroxides derived from (cyolo) aliphatic ketones, such as methyl ethyl ketone peroxide, .. . . . . .
acetone peroxide, methyl amyl ketone peroxide, cyclopentanone peroxide, and on the other hand, benz~yl peroxide and chlorinated derivatives thereof such as 2,4-dichlorobenzoyl peroxide.
The former category is incorporated in the paste in an amount not higher than 30~0 by weight, benzoyl peroxide or the nuclear-chlorinated derivatives thereof, in an amount of ;~

not more than 50~0 by weight. As solvènts for pastes containing .
the former category of organic peroxides are recommended liquid or wateræoluble aliphatic polyoxyalkanes and alkyl esters. As solvents for benzoyl peroxide-containing pastes are mentioned compounds such as precipitated, finely divided silica, alkyl cellulose, etc., which compounds may form a gel with the ! _ water contained in the paste. Mention is also made of com-pounds known under the name of detergent. The compositions ~ - .

-~05365Z
described in U.S, Patent 3,507,800 have the disadvantage that they are pasty.
They are, therefore, less suitable to be used as catalyst in (co)polymerization reactions carried out in a closed system in order to prevent the escape of monomers, e.g., vinyl chloride, detrimental to health. In such techniques, the composition to be used should be pumpable.
DESCRIPTION OF THE INVENTION
It has now been found that if an aqueous suspension of at least about 20 weight % of organic peroxide solid at about 20C is made to contain a combination of at least 0.2%
by weight of a nonionic emulsifier with an HLB-value not higher than I2.5 and at least 0.2% by weight of a non-ionic ., , - emulsifier with an HLB-value not lower than 12.5 or a combin-ation of at least 0.2% by weight of a non-ionic emulsifier with an HLB-value not higher than 12,5 and at least 0,01% by weight of an anionic emulsifier, then there is obtained a pumpable aqueous suspension which may contain a high proportion of organic peroxide which is solid and chemically stable at about 20C, ~ Broadly, the invention relates to a pumpable, stable, ., aqueous suspension comprising at least about 20 weight % of an organic peroxide which is solid at about 20C, at least about ~i 0.2 weight % of a nonionic emulsifier having a maximum HLB-`' value of 12,5 and an emulsifier selected from the group con-~, sisting of nonionic emulsifiers having a minimum HLB-value of 12.5, and anionic emulsifiers, said nonionic emulsifier of minimum HLB-value of 12.5 present in an amount of at least about 0,2 weight %, and said anionic emulsifier present in an , 30 amount of at least about 0.01 weight %, By HLB-value is to be understood the hydrophilic- -~
lipophilic balance as worked out by the Atlas Powder Company .,~, , ''t - 3 ~ .

and published in "The Atlas H1B-System, a time saving guide to emulsifier selection". These HLB-values are in the range of 1 to 30.
Examples of nonionic emulsifiers to be used in the process according to the invention are summarized in the following Table N.
TAB~E N
Trademark Chemical Name HLB-value Surfonic N-10 nonylphenol polyethylene oxide 3.4 ether Akyporox nonylphenol polyethylene oxide 4.4 ether : Elfapur ~M-30 fatty alcohol polyethylene oxide 7.5 ether ` Tergitol 15-S-3 linear alcohol polyethylene 8.0 ,: oxide ether Span 20 sorbitan monolaurate 8.6 Tween 81 sorbitan monooleate polyethylene 10.0 . oxide ether Tergitol NP 15 nonyl phenyl polyethylene oxide 10.0 . ethqr Elfapur N-50 nonyl phenyl polyethylene oxide 10,0 ether ~ Elfapur N-70 nonyl phenyl polyethylene oxide 11.7 ., ether , Elfapur IM-75-S fatty alcohol polyethylene oxide 12.3 ether , Elfapur N-90 nonyl phenol polyethylene oxide 12,9 ether Terg,,tol NP-33 nonyl phenol polyethylene oxide 14.4 .i , ether .~ Tergitol 15-S-12 linear a~icohol polyethylene oxide 14.5~ ether `~ Tergitol NP-25 nonyl phenol polyethylene oxide 14.7 .~ Elfapur N-150 nonyl phenol polyethylene oxide 15.0 ~i Tergitol NP-40 nonyl phenol polyethylene oxide 16,0 ~ Tween 20 sorbitan monolaurate polyethylene 16,7 ,~ oxide ether :, ~ - 4 -It will be clear that within the scope of the invention, also mixtures may be used of nonionic emulsifiers having a total HLB-value not higher than or not lower than 12.5 This total HLB-value can be calculated from the HLB-values of the individ-ual emulsifier and their weight ratios As examples of anionic emulsifiers to be added in combination with an emulsifier or emulsifier mixture with an HLB-value not higher than 12.~ may be mentioned:
Na-dodecylbenzene sulphonate, Na-laurylalcohol sulphate, dialkyl esters of Na-sulphosuccinate, Na-di(2-ethylhexyl) - phosphate, Na-tetradecyl sulphate, NH4-linear alcohol - polyethylene oxide ether sulphate, Na-olefin sulphate.
An aqueous suspension according to the invention was considered pumpable when it had a viscosity of not more than .~.
500 poises Preference, however, is given, to suspensions having a viscosity of not more than 100 poises.
In order to prevent that the solid organic peroxides present in the suspension according to the invention can no longer be homogeneously distributed in the aqueous phase after segregation, if any, it is recommended that in the SuSpenSiQnS
; according to the invention there should be incorporated thick-i eners in such amounts that after segregation the solid organic peroxide can again be homogeneously distributed in the aqueous .phase and preferably in such amounts that such segregation is prevented, ~As thickeners may be used water-soluble polymers ~such as carboxymethyl cellulose, methyl cellulose, hydroxy ~ethyl cellulose, hydroxypropyl cellulose and other water-soluble cellulose derivatives, polyvinyl alcohol, polyvinyl-3 pyrrolidone, polyacrylic acid, carboxyvinyl polymers, gelatin, ~.
i~starch, agar, etc. Depending on the type of thickener, the desired viscosity of the ready suspension, the nonionic . .

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emulsifiers used and the solid peroxide, the amounts of thickener to be incorporated in the suspension according to the invention may be in the range of 0.05 to lO~o by weight, and preferably in the range of 0.2 to 4% by weight.
The suspensions according to the invention may be prepared by vigorously mixing and homogenizing the components with the aid of appropriate mixing equipment.
As examples of peroxides solid at a temperature of about 20C that may be incorporated in`the suspension according to the invention may be mentioned:
1. solid aromatic diacyl peroxides, such as di-benzoyl peroxide and nuclear-substituted derivatives thereof such as bis~o-methylbenzoyi) peroxide, bis(o-methoxybenzoyl) peroxide, bis(o-ethoxybenzoyl) peroxide, bis(o-chlorobenzoyl) peroxide;
2 solid aliphatic diacyl peroxides, such as didecanoyl peroxide, dilauroyl peroxide and dimyristoyl peroxide;
3. solid ketone peroxides such as bis(l-hydroxy-~ 20 cyclohexyl) peroxide, l-hydroxy-l-hydroperoxy-dicycloperoxide, ;~ bis-(l-hydroperoxycyclohexyl) peroxide;
4, solid aldehyde peroxides such as bis(l-hydroxy- ~-heptyl) peroxide~
~ , solid dialkyl peroxides and diaralkyl peroxides ` such as dicumyl peroxide, 1,3- and 1,4(di.tert. butylperoxy-`. isopropyl) benzene;
-~¦ 6. solid peresters such as mono-tert. butyl permaleate di-tert.-butylperoxyhexahydro terephthalate, di-tert.butylperoxyadipate, di-tert. butylperoxyterephthalate, di-tert, butylperoxyphthalate, mono-tert. butylperoxyphthalate;
7 solid perketals such as 2,2-bis(4,4-detert butylperoxycyclohexyl) propane, 1,1-ditert.butylperoxy-4-tert.

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~05365Z
butylcyclohexane;
8 solid hydroperoxides such as 2,5-dihydroperoxy-2,5-dimethylhexane, 1,3-bis( ~-hydroperoxyisopropyl)benzene, 1,4 bis~ hydroperoxyisopropyl) benzene;
9. preferably, however, solid peroxydicarbonates such as dimyristyl peroxydicarbonate, dicetyl peroxidicarbonate, distearyl peroxydicarbonate, bis(4-tert.butylcyclohexyl) peroxydicarbonate, bis(4-tert.amylcyclohexyl) peroxidicarbonate, dicyclohexyl peroxydicarbonate and dibenzyl peroxydicarbonate.
The invention will be elucidated in the following . examples. The viscosity values mentioned in these examples are in poises and were measured with~a Brookfield rotational type viscometer, model HB, at a speed of 5 revolutions per minute of the measuring spindle.

In a solution of 10 g. of methyl cellulose and 5 g.
of nonionic emulsifier with an HLB-value of 15,0 (Elfapur N-150*) in 313 ml. of water there were distributed 667 g of a dibenzoyl peroxide wetted with water (25% H20). The mass was homogenized with the aid of a triple-roller mill and a highly viscous, non-pourable suspension was obtained To this suspenslon there `~ was added 5 g. of a nonionic emulsifier with an HLB-value of 10.0 (Elfapur N-50*). A pourable, pumpable aqueous suspension with a viscosity of 30 poises was obtained. Its composition was as follows: ;
50% dibenzoyl peroxide 1 48% water ;~ 0 5% nonionic emulsifier, HLB = 15.0 0 5% nonionic emulsifier, HLB = 10.0 1 30 1% methyl cellulose t * Trademark , .~
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In a solution of 5 g. of hydroxypropyl methyl cellulose and 5 g. of nonionic emulsifier with a HLB-value of 14 7 (Tergitol NP-35*) in 318 ml of water there was dispersed 667 g. of a dibenzoyl peroxide wetted with water (25~o H20), The mass was homogenized with the aid of a triple-roller mill and a highly viscous non-pourable suspension was obtained.
To this suspension there was subsequently added 5 g. of a non-ionic emulsifier with an HLB-value of 10.0 (Tergitol NP-15*).
A pourable, pumpable aqueous suspension was obtained having a viscosity of 14 poises and the following composition:
50~o dibenzoyl peroxide 48,5% water 0.5% nonionic emulsifier, HLB 14.7 . 0.5% nonionic emulsifier, HLB 10.0 0,5% hydroxypropyl methyl cellulose EXAMPLE ~
In a solution of 5 g of hydroxypropyl methyl cellulose and 5 g. of nonionic emulsifier with an HLB-value 20 of 10.0 (Elfapur N-50*~ in 323 ml. of water there was homo-geneously distributed 667 g. of a dibenzoyl peroxide wetted ' with water (25% H20). A high viscous, non-pourable suspension of the following composition was obtained:
~ 50% dibenzoyl peroxide :' 49% water 0,5% nonionic emulsifier, HLB = 10.0 0~5% hydroxypropyl methyl cellulose The suspension was divided into three portions of --~ equal amounts by weight, after which to each portion there was '~ 30 added a certain amount of sodium lauryl alcohol sulphate as anionic emulsifier. Subsequently, of each portion, the viscosity * Trademark ..... .. . ..

was measured, The added amounts of sodium lauryl alcohol sulphate and the measured viscosities are listed in the following table, Na-~auryl Alcohol SulphateViscosity in Poises in % b~ Wei~ht 0,02 640 0,25 380 0.1 55 EXAMP~ES 4 - 11 Suspension having the compositions and viscosities given in the following table were prepared in the same way as ~ -described in Example 1, When only one of the two emulsifiers was used, always a pasty or highly viscous suspension was obtained, Addition of the other emulsifier resulted in a con-siderable decrease in viscosity, ,~ .

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EXAMP~E 12 In a solution of 10 g. of methyl cellulose and 10 g.
of nonionic emulsifier with an HIB-value of 15.0 (Elfapur N-150*) in 560 ml. of water there were distributed 360 g. of dilauroyl peroxide and 50 g. of a bis(o-methylbenzoyl) peroxide wetted with water (20% H20), The mass was homogenized to a viscous suspension having a viscosity of ~300 poises with the aid of a triple-roller mill. Subsequently, 10 g. of a nonionic emulsifier with an HLB-value of 10.0 (Elfapur N-50* ) were added, with stirring. As a result, the viscosity dropped to 39 poises. The composition of this pourable, pumpable sus-pension was as follows:
36% dilauroyl peroxide 4% bis(o-methylbenzoyl) peroxide ; 57% water 1% nonionic emulsifier, HLB = 15,0 . 1% nonionic emulsifier, HLB = 10.0 1% methyl cellulose -In the same way as described in Example 12, a sus-pension of dilauroyl peroxide and bis(4.tert butylcyclohexyl) - -peroxydicarbonate was prepared having the following composition.
36~o dilauroyl peroxide 4~0 bis(4-tert.butylcyclohexyl) peroxydicarbonate 58~o water 0.5% nonionic emulsifier, HLB = 15.0 i~ 0.5~o nonionic emulsifier, HLB = 10 0 ;~ 1% methyl cellulose Before the addition of the nonionic emulsifier HLB =
10,0 (Elfapur N-50*) ~ the suspension was not pourable. After * Trademark , the addition thereof, the viscosity dropped to 31 poises.

In a solution of 5 g. of polyvinyl alcohol and 20 g.
of a nonylphenyl polyethylene oxide with an H1B-value of 14.7 (Tergitol NP-35*) in 665 ml. of water there was homogeneously distributed 300 g, of dicetylperoxydicarbonate, The resulting paste was divided into 5 equal portions after which to each portion there was added 4 g, of the nonionic emulsifiers with an HLB-value < 12.5. The aqueous suspensions obtained were compared as followsz 30.0% dicetylperoxycarbonate 0,5% polyvinyl alcohol 65.5% water 2,5~o emulsifier, HLB-value 14.7 2.0% emulsifier, HLB-value < 12,5 The added emulsifiers with HLB-values of 14.7 and the measured viscosities of the resulting suspensions are listed in th,e following table.
Added Nonionic Emulsifier HIB-Value ViscositY
20Surfonic N-10* 3,4 54 , -; Akyporox NP-15* 4,4 48.5 ~, Tergitol 15-S-3* 8.0 32.5 -~ Tergitol NP-15* 10.0 9 Elfapur N-70* 11.7 22 The suspensions obtained were stable. The suspensions obtained with the use of Elfapur N-70* had thixotropic properties, .
i EXAMPLE 1 .. . .
~ In a solution of 5 g. of polyvinyl alcohol in 582 ml, -~ of water there was dispersed 600 g, of bis(4-tert.butylcyclo-'¦ 3 hexyl) peroxydicarbonate and 6 g, of a nonionic fatty alcohol--~ * Trademark ,................................................................. .
, polyethylene oxide having an HIB-value of 7,5 (Elfapur ~M-30*).
The resulting non-pourable paste was divided into 6 equal portions, after which to each portion 1 g, of a nonionic emulsifier with an H1B-value between 12 and 16.5 was added.
The resulting aqueous suspensions were composed as follows:
50,0% bis(4-tert,butylcyclohexyl) peroxydicarbonate 0.5% polyvinyl alcohol 48,5% water O.5% emulsifier, HLB-value 7.5 10 0.5% emulsifier, HLB-value 12-16.5 The added emulsifiers and the measured viscosities of the suspensions obtained are listed in the following table, Added Nonionic Emulsifier HLB-Value ViscositAv Elfapur ~M-75-S* 12,3 stiff, paste ;
Elfapur N-90* 12,9 10 Tergitol NP-33* 14,4 4 Tergitol 15-S-12*14,5 4 ; Elfapur N-150* 15.0 3 Tergitol NP-40* 16,0 3 -In the same way as described in Example 1, suspensions were prepared of the composition~given in the following table, Of these compositions, the stabilities and the viscosities were measured, The results obtained are also given in the . following table, , ~ , .

~l 30 * Trademark .,j -., ,.~

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,: ., . . . ~ ~ . -. - , , r Composition Percent b~ wei~ht bis(4-tert.butyl p.o. 50 50 50 50 dicarbonate) polyvinyl alcohol - 1 2 3 nonylphenol-poly- 0.5 0.5 0.5 0.5 ethylene oxide, XlB 10.0 nonylphenyl-poly- 0.5 0.5 0.5 0.5 ethylene oxide, HIB 14.7 water 49 4O 47 46 viscosity 9 10 43 135 -Segregation after 1 2 2 24 hrs. Strong Moderate Slight None 170 hrs. Strongl Strongl Moderate2 None 1 composition can no longer be homogenized 2 composition can be homogenized To a suspension obtained by homogenizing 5 g. of hydroxyethyl cellulose, 585 ml. of water, 400 g. of bis(4-tert.
butylcyclohexyl) peroxydicarbonate and 3 g, of a fatty alcohol alkyl polyethylene oxide ether with an HLB-value of 7.5 ` (Elfapur ~M-30*) there was added as anionic emulsifier, sodium-dodecylbenzene sulphate in an amount of 0.01% by weight. Next, the viscosity was measured of suspensions containing other ..
amounts of Na-dodecylbenzene sulphonate. The added amounts of Na-dodecylbenzene sulphonate and the measured viscosities in ;~ poises are summarized in the following table:
30 ~ by Weight Na-Dodecylbenzene SulPhonate Viscosit~
~ 0,01 106 s 0.015 48 0,02 35 , 0.025 32 * Trademark . .
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In a solution of 3 g. of hydroxyethyl cellulose in 652 ml. of water there was dispersed 300 g. of dicetyl peroxydicarbonate and 25 g of sorbitan monolaurate, a nonionic emulsifier with an HLB-value of 8.6 (Span 20*). The resulting, non-pourable, pasty mass was mixed with 20 g of sorbitan monolaurate polyethylene oxide ether, a nonionic emulsifier with an HLB-value of 16 7 (Tween 20*). A pourable pumpable suspension having a viscosity of 170 poises was obtained.
Its composition was as follows:
30.0% dicetyl peroxydicarbonate 0 3% hydroxyethyl cellulose ; 65.2% water 2 5~o sorbitan monolaurate, HLB-value 8.6 2 0% sorbitan monolaurate polyethylene oxide ether HLB-value 16 7 In the same way as described in Example 5, a suspension of the following composition was prepared.
~ 2030.0% dicetyl peroxydicarbonate ; 0,5% methyl cellulose 66.6% water 2.0~o sorbitan monoolate polyethylene oxide ether HLB-value 10.0 (Tween 81*) 0,9% sorbitan monolaurate, HLB-value 16.7 (Tween 20*) Its viscosity was 22 poises.

, EXAMP~E 20 . j .
In a solution of 5 g. of hydroxyethyl cellulose and ; 20 g. of a nonylphenol polyethylene oxide ether with an HLB-30value of 15.0 (Elfapur N-150*) in 555 ml. of water, there was -. * Trademark . .

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A_ . . . . : , ' ..
,: . ,~ . . ' ' ' ' 1053~52 homogeneously distributed 400 g. of dicyclohexyl peroxidicar-bonate.
To the resulting pasty mass there was added 2 0 g. of a nonylphenol polyethylene oxide ether with an HLB-value of 10.0 (Elfapur N-50*). A pourable, pumpable suspension having a viscosity of 54 poises was obtained. Its composition was as follows:
40.0% dicyclohexyl peroxydicarbonate 0.5% hydroxyethyl cellulose 55.5% water 2 0% nonylphenol polyethylene oxide ether, HLB 1.50 2.0% nonylphenol polyethylene oxide ether, HIB 10.0 In a solution of 5 g. of methyl cellulose and 20 g.
(Elfapur N-150*) of a nonylphenol polyethylene oxide ether with ! an HIB-value of 15.0 in 655 ml. of water there was homogeneously... . .
distributed 300 g. of distearyl peroxydicarbonate. To the -resulting pasty mass there was added 20 g. of a nonylphenol polyethylene oxide having an HLB-value of 10Ø A pourable, . ~ , - .
pumpable suspension having a viscosity of 75 poises was ~-obtained. Its composition was as follows: -30.0~ distearyl peroxydicarbonate 65.6% water ~ .
,:
'~ 0.5~ methyl cellulose ' 2,0% nonylphenol polyethylene oxide ether, HLB-value 1 2,0~ nonylphenol polyethylene oxide ether, HLB-value 3 10.0 The suspensions according to the invention containing a peroxydicarbonate are particularly suitable for the (dis)-continuous polymerization of vinylchloride. It was found ~` * Trademark .
`i - 17 -~c 1~5365Z
that there was far less reactor fouling than when in a poly-merization under the same conditions use was made only of a solid peroxydicarbonate.

In a solution of 3 g of hydroxyethyl cellulose and 20 g of a nonylphenyl polyethylene oxide with an HIB-value of 15 0 (Elfapur N-150*) in 657 ml. of water there was homo-geneously distributed 300 g. of dicetyl peroxydicarbonate To the pasty mass there was subsequently added 20 g. of a non-ylphenyl polyethylene oxide having an HLB-value of 10.0 (Tergitol NP-15*). The resulting suspension had a viscosity of 13 poises and did not show any segregation after four weeks' storage at 22C, 0 53 g. of this suspension was used for the suspension polymerization of 200 g. of vinyl chloride at 55C in a glass autoclave.
After termination of the polymerization, the degree of fouling of the reactor was measured by screening the poly-vinyl chloride with a sieve having a mesh width of 500 ~ ;
and determining the amount of material retained by the sieve.
This amount was 0. 33%. In a similar determination, in which, ¦ however, 0 16 g of pure, solid dicetyl peroxydicarbonate was used, the amount of material retained by the sieve was found to be 3,1~o by weight.
The invention is not limited to the embodiment des-cribed above. Within the scope of the invention, other applications of the suspension according to the invention are conceivable, such as the polymerization of acrylates and the copolymerization of styrene.
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Claims (9)

The embodiments of the invention in which an exclusive property or privilege is claimed are defined as follows:-
1. A pumpable, stable, aqueous suspension comprising at least about 20 weight % of an organic peroxide which is solid at about 20°C, at least about 0.2 weight % of a nonionic emulsifier having a maximum HLB-value of 12.5 and an emulsifier selected from the group cnnsisting of nonionic emulsifiers having a minimum HLB-value of 12.5, and anionic emulsifiers, said nonionic emulsifier of minimum HLB-value of 12.5 present in an amount of at least about 0 2 weight %, and said anionic emulsifier present in an amount of at least about 0.01 weight %.
2. A composition as in claim 1 wherein the organic peroxide is a peroxydicarbonate.
3. A composition as in claim 1 additionally containing a thickening agent.
4. A composition as in claim 3 containing 0.05 to 10.0 weight % of thickening agent based on the total weight of the composition.
5. A composition as in claim 1 characterized in that the nonionic emulsifier with maximum HLB of 12.5 is nonylphenol polyethylene oxide ether, a linear alcohol polyethylene oxide ether, a fatty alcohol polyethylene oxide ether, sorbitan mono-laurate or sorbitan monooleate polyethylene oxide ether.
6. A composition as in claim 1 characterized in that the nonionic emulsifier having a minimum HLB of 12.5 is a nonylphenyl polyethylene oxide ether, or a linear alcohol polyethylene oxide ether.
7. A composition as in claim 1 wherein the anionic emulsifier is sodium-dodecylbenzene suphonate.
8. A composition as in claim 3 wherein the thickening agent is polyvinyl alcohol, hydroxyethyl cellulose, or methyl cellulose.
9. A process for the polymerization of ethylenically unsaturated monomers which comprises reacting said monomers in the presence of the aqueous suspension defined by claim 1.
CA246,992A 1975-03-14 1976-03-02 Stable, pumpable, aqueous suspensions of organic peroxides Expired CA1053652A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NL7503051A NL186816C (en) 1975-03-14 1975-03-14 METHOD FOR PREPARING A PUMPABLE ORGANIC PEROXIDE AND EMULGATOR CONTAINING AQUEOUS SUSPENSION
NL7507859A NL179375C (en) 1975-07-02 1975-07-02 METHOD FOR PREPARING A PUMPABLE ORGANIC PEROXIDE AND EMULGATOR CONTAINING AQUEOUS SUSPENSION

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CA1053652A true CA1053652A (en) 1979-05-01

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JP (1) JPS6010029B2 (en)
AR (1) AR208425A1 (en)
AU (1) AU501457B2 (en)
BR (1) BR7601489A (en)
CA (1) CA1053652A (en)
DE (1) DE2610181C2 (en)
ES (1) ES453345A1 (en)
FR (1) FR2303811A1 (en)
GB (1) GB1495894A (en)
IT (1) IT1057024B (en)
NO (2) NO146778C (en)
SE (1) SE410316C (en)

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NO760830L (en) 1976-09-15
SE410316C (en) 1986-01-20
SE7602213L (en) 1976-09-15
AU501457B2 (en) 1979-06-21
FR2303811A1 (en) 1976-10-08
SE410316B (en) 1979-10-08
JPS51125302A (en) 1976-11-01
DE2610181A1 (en) 1976-09-23
FR2303811B1 (en) 1980-03-28
NO146778C (en) 1986-06-12
NO146778B (en) 1982-08-30
IT1057024B (en) 1982-03-10
ES453345A1 (en) 1977-11-16
JPS6010029B2 (en) 1985-03-14
AR208425A1 (en) 1976-12-27
GB1495894A (en) 1977-12-21
AU1184676A (en) 1977-09-15
BR7601489A (en) 1976-09-14
NO800003L (en) 1976-09-15
US4039475A (en) 1977-08-02
DE2610181C2 (en) 1986-01-16

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