Method for producing block-shaped polymethacrylimide foamed materials

BACKGROUND OF THE INVENTION

1. Field of the Invention

The invention relates to a method for producing polymethacrylimide foamed materials as well as blocks, plates and the like of such polymethacrylimide foamed materials as well as the shaped articles obtained as intermediate products from the copolymer of methacrylic acid and methacrylonitrile.

2. Discussion of the Background

It is known how to produce polymethacrylimide foamed materials in the form of blocks. The first step is production of a preliminary product, which is already obtained in appropriate plate shape, from methacrylic acid and methacrylonitrile by copolymerization. The copolymer is then cyclized to the imide. An expanding agent present in the reaction mixture ensures appropriate foam formation when heated.

Heretofore, direct production of suitable polymer plates has been possible only up to a thickness of 30 mm. Since it is absolutely necessary to ensure a regular and reliable polymerization sequence, cooling and heating must be applied alternately during polymerization, especially because the polymerization can no longer be controlled and irregular structures are formed if heating is too intensive. These alternating cooling and heating phases are naturally cumbersome, and also entail high energy and water consumption.

In addition, polymer plates with thicknesses of only up to 30 mm suffer from numerous disadvantages. For example, if foamed blocks of relatively large thickness are needed, a plurality of foamed plates must be cemented together. Moreover, very large amounts of waste are produced from the edge regions during manufacture.

In German Patent No. 1817156 there is already described a method in which foamable plastics are produced in plate form by polymerizing mixtures of methacrylonitrile and methacrylic acid between two glass plates sealed with a flexible cord. An expanding agent such as formamide or monoalkylformamide is already added to the starting mixture. Radical sources are also added, in the form, for example, of a two-component mixture of tert-butyl perpivalate and benzoyl peroxide.

The polymerization takes place at temperatures of, for example, 40, 45 or 48° C., and it lasts about 15 to 40 hours. The product is then tempered at about 100° C. and subsequently heated to 170 to 300° C. Cyclization to imide and foam formation take place at the latter temperatures.

It is difficult to ensure regular polymerization, because the temperature can very easily exceed the specified temperature. Temperature fluctuations must therefore be controlled very accurately and compensated for by alternating cooling or heating phases.

Plates thicker than 30 mm cannot be produced by this method, since temperature elevations occur repeatedly and, because of the relatively poor thermal conductivity of the polymerization mixture, the heat generated cannot be dissipated rapidly enough. Uncontrollable and unmanageable temperature elevations naturally lead to further increase of radical formation, and so the reaction very easily runs out of control.

A method similar to that of German Patent No. 1817156 is described in European Patent 0356714 A1. As the radical source there is used, for example, azobisisobutyronitrile, and 0.1 to 10 wt % of electrically conductive particles is added to the mixture to be polymerized.

The aforesaid problems also occur in this method, and the polymer plates obtained according to Example 1 of this European Patent Application have a thickness of only 25 mm.

Although numerous methods for producing foamed plates of polymethacrylimides are already known, a need still exists for improved methods of producing same and also for improved polymethacrylimide plates.

In particular, therefore, a need exists for thick foamed blocks and especially for a method with which such blocks can be produced without having to cement a plurality of blocks together.

SUMMARY OF THE INVENTION

The object of the invention is therefore to provide such blocks, especially in plate form, as well as a method for producing the same, with which a uniform block with thicknesses up to 80 mm and more can be produced in one step, which permits a reliable and controlled polymerization process and which operates with reduced water and energy consumption and which yields blocks in which relatively little waste is produced during manufacture. Another object of the invention is to provide an appropriate method in which the tempering bath, especially the tempering water bath, can be operated largely with constant temperature.

This object is achieved by a method for producing block-shaped polymethacrylimide foamed materials by copolymerization of methacrylic acid and methacrylonitrile as well as further copolymerizable monomers if necessary in the presence of radical-forming initiators, postpolymerization and cyclization of the copolymer to polyimide and transformation to a foamed material, which is characterized in that the copolymerization is performed in the presence of a mixture comprising at least three initiators with graduated half lives.

The subject matter is therefore a method according to the teaching of claim

1

. Further advantageous embodiments are described in claims

2

to

7

, and correspondingly produced blocks are described in claims

8

to

9

. Further subject matter of the invention is methods according to claim

10

, polymer plates according to claim

11

and the use according to claim

12

.

BRIEF DESCRIPTION OF DRAWINGS

FIG. 1

shows the temperature dependence of the half-life of initiators listed in Table 2.

FIG. 2

shows the temperature dependence of the half-life of initiators listed in Table 2.

FIG. 3

shows the temperature dependence of half-lives of azo compounds listed in Table 3.

FIG. 4

shows the temperature dependence of half-lives of azo compounds listed in Table 3.

DETAILED DESCRIPTION OF THE INVENTION

In connection with the invention, graduated half lives means that the at least three initiators each have different half lives at a given temperature or have the same half life, but in different temperature ranges. Preferably there are used initiators which each have a half life of one half hour in temperature ranges that are at least 10° C. apart.

In a particularly advantageous embodiment of the inventive method, there is used an initiator mixture which comprises agents that decompose at low temperature, medium temperature and high temperature and that have half lives of 1 hour in the ranges of 40 to 80, 80 to 110 and 110 to 200° C., preferably 110 to 150° C.

Preferably there are used initiator mixtures which comprise at least four initiators, each with a half life on the order of one hour in different temperature ranges.

The proportion of initiator mixture used can be varied within relatively broad limits; in this way the polymerization time can be controlled and also the polymerization temperature can be influenced by the proportion of initiators used. The quantities used in connection with the invention are expressed as weight parts of initiator per 100 weight parts of monomer. It is advantageous to use a total proportion of initiator mixture ranging from about 0.2 to 0.3 weight parts per 100 weight parts of monomer, preferably 0.21 to 0.24 weight parts.

The weight ratio of the individual initiators relative to each other in the initiator mixture can also be varied within relatively broad limits; preferably the weight ratio of the individual initiators relative to each other ranges from 1:1 to 1:10, preferably 1:1 to 1:4. Suitable proportions and mixing ratios can be determined by simple preliminary experiments.

Further subject matter of the invention are foamed blocks, especially foamed plates with a thickness of up to 80 mm, which are obtainable according to one of the foregoing methods.

In the first step of the production of block-shaped foamed materials, there are prepared monomer mixtures containing methacrylic acid and methacrylonitrile as main constituents, preferably in a mole ratio of between 2:3 and 3:2. In addition, further conomomers can be used, such as esters of acrylic or methacrylic acid, styrene, maleic acid or itaconic acid, etc., the anhydrides thereof, vinylpyrrolidone, etc. The proportion of such comonomers should be no more than 30 wt %, preferably no more than 10 wt % of the two main constituents. Small proportions of cross-linking monomers such as allyl acrylate can also be used. Preferably, however, the proportions should be at most 0.05 to 1 wt %. The polymerization mixture also contains at least three initiators, each of which has a half life on the order of one hour in different temperature ranges. It is advantageous to use appropriate initiators from at least four temperature ranges. Examples of suitable temperature ranges are 50 to 57° C. for the first range, 60 to 80° C. for the second range, 85 to 105° C. for the third range and 115 to 125° C. for the fourth range. As initiator in each of the individual temperature ranges, it is possible to use a single compound as initiator, but it is also possible to use two or more initiators with the appropriate half lives in the corresponding temperature ranges.

As suitable initiators for use according to the invention in a mixture comprising at least three initiators, there can be used standard initiators such as are used for radical generation in radical-initiated polymerization. These include compounds such as organic peroxides, such as dicumyl peroxide, peroxydicarbonates, such as diisopropyl peroxydicarbonate, peresters, such as tert-butylperoxy 2-ethylhexanoate and the like. Further compound types that can form radicals are also suitable in connection with the invention. They include in particular azo compounds such as azobis(isobutyronitrile) and azobis(2,4-dimethylvaleronitrile).

Initiator mixtures that are particularly suitable in connection with the invention are those whose components are selected from the following initiators: azobis(isobutyronitrile), t-butyl peroctoate, t-butyl perbenzoate, t-butyl perpivalate, azobis(2,4-dimethylvaleronitrile), t-butyl perneodecanoate, dibenzoyl peroxide, bis(4-t-butylcyclohexyl) peroxydicarbonate, cumylperoxy neodecanoate, 1,4-di(2-neodecanoylperoxyisopropyl)benzene and the like.

Table 1 lists suitable initiators, together with the temperatures for half lives of 10 hours, 1 hour and 1 minute, as well as the half lives in hours for a series of temperatures. Table 2 shows initiators who's dependence of half life on temperature is illustrated in

FIGS. 1 and 2

. It is a simple matter to compose initiator mixtures by means of the graphs of

FIGS. 1 and 2

.

Table 3 lists azo compounds which are suitable as initiators in connection with the invention.

FIGS. 3 and 4

graphically illustrate half lives of several azo compounds listed in Table 3.

The half lives of the usable initiators generally already are given by the manufacturer. They can easily be determined analytically, for which purpose benzene has generally proved suitable as the solvent. The determination is generally performed with 0.1 molar solution.

The mixture for copolymerization also contains expanding agents, which either decompose or evaporate at temperatures of about 150 to 250° C., and in the process form a gas phase. Examples of nitrogen-containing compounds for use as expanding agents are urea, monomethylurea or N,N′-dimethylurea, formamide or monomethylformamide. Further nitrogen-free expanding agents are formic acid, water or monohydric aliphatic alcohols, especially those with three to eight carbon atoms. The expanding agents are generally used in proportions of 0.5 to 8 wt % relative to the monomers used.

Polymerization is expediently carried out in block form. During the production of blocks, for example in flat layers with thicknesses of up to 80 mm, the monomer mixture is disposed between two glass plates, which are sealed at their respective edges and form a kind of flat chamber. This flat chamber is surrounded by a water bath adjusted to the desired polymerization temperature.

The polymerization can be achieved largely or over broad ranges under isothermal conditions, or in other words at constant water-bath temperature. In many cases it is possible to keep the water-bath temperature constant from the beginning to the end of polymerization. If necessary, however, the water-bath temperature can also be kept constant for a long time at first and raised after a specified time, in order to perform part of the polymerization at a higher temperature.

The water-bath temperature can also be kept constant in this next polymerization phase, which is performed at a higher temperature.

The chosen water-bath temperature depends on the thickness of the polymerization chamber and on the formula used for polymerization. In this connection it is generally advantageous to shift the polymerization temperature and thus also the water-bath temperature to lower values with increasing density of the plate to be produced.

The appropriate temperature for the formula and thickness can be optimized in each case by simple preliminary experiments.

It is self-evident that the temperature must be adjusted to the chamber thickness and the formula such that the heat liberated during polymerization can be adequately dissipated without allowing undesired temperatures to develop in the polymerization mixture during polymerization. After completion of the polymerization process, which is controlled by the surrounding water bath, postpolymerization is performed in an oven. Postpolymerization is generally performed at temperatures of 38 to 140° C. In general, 10 to 1000 hours is sufficient for final polymerization in the tempering oven.

After completion of polymerization, the block is heated to a temperature of about 180 to 250° C., at which temperature cyclization to the imide structure and foam formation take place. Times of 3 to 5 hours are usually sufficient for this thermal posttreatment.

The blocks obtained in the process are characterized by a homogeneous regular structure.

Further subject matter of the invention is a method for producing polymer plates by copolymerization of methacrylic acid and methacrylonitrile as well as further copolymerizable monomers if necessary in the presence of radical-forming initiators and postpolymerization, characterized in that the copolymerization is performed in the presence of a mixture comprising at least three initiators with graduated half lives.

These polymer plates are formed as intermediate products during production of the block-shaped methacrylimide foamed materials according to the invention. Further subject matter of the invention is polymer plates obtainable by the method specified hereinabove.

It was particularly surprising that, with the inventive method, it is possible to perform the polymerization isothermally, or in other words at constant temperature, and thus obtain polymer blocks which have thicknesses of up to 80 mm and which exhibit a uniform properties profile through the entire thickness of the block, thus indicating regular homogeneous polymerization. The foamed blocks produced therefrom can be manufactured as such, so that only very little waste is produced at the edge regions. In this way it is possible to produce shaped articles of appropriate thickness using only a single block, whereas a plurality of blocks cemented together was formerly necessary for this purpose. The resulting blocks or plates, which are foamed in one piece, preferably have thicknesses of 80 to 300 mm.

The foamed plates or foamed blocks according to the invention are very valuable materials and can be used in particular as components in aircraft construction. The polymer blocks produced according to the invention are characterized by extremely regular structure, can be stored indefinitely and, if necessary, can be transformed to foamed plates from case to case by appropriate heating.

EXAMPLES

The invention will be explained in more detail by means of the following examples:

Example 1

A mixture of 61 parts of methacrylic acid, 39 parts of methacrylonitrile, 4.7 parts of formamide and 4.2 parts of 2-propanol and an initiator mixture of 0.3 parts of t-butyl perpivalate, 0.04 parts of t-butyl per-2-ethylhexanoate, 0.07 parts of t-butyl perbenzoate and 0.077 parts of cumyl perneodecanoate is polymerized for 66 hours at a water-bath temperature of 38° C. between two glass plates spaced 23 mm apart and sealed by a sealing cord, after which postpolymerization is performed for 24 hours in an oven at a temperature of 115° C. Regular plates are obtained. During the polymerization, which is controlled by the water bath, temperature fluctuations are practically zero or only slight, and do not necessitate readjustment of the water-bath temperature.

The obtained plates can be transformed without problems to foamed plates by heat treatment at a temperature of 170 to 200° C.

Example 2

A mixture identical to that of Example 1 is polymerized in a flat chamber whose glass plates are spaced 30 mm apart. In this case the water bath is kept at 33° C. for 92 hours, at 33 to 38° C. for 10 hours and at 38° C. for 14 hours. Tempering in the oven at temperatures of 115° C. is performed for 40 hours.

The plates have uniform structure and can be transformed without problems to foamed materials.

Example 3

A composition identical to that of Example 1 is polymerized in a flat chamber whose glass plates are spaced 50 mm apart. The water bath is kept at 28° C. for 198 hours, at 28 to 37° C. for 30 hours and at 37° C. for 24 hours. Postpolymerization at a temperature of 115° C. is performed for 50 hours.

Examples 4 to 6

In the following examples, a polymerization mixture with the following composition is polymerized: 56 parts of methacrylic acid, 44.0 parts of methacrylonitrile, 1.0 parts of formamide, 3.3 parts of 2-propanol, 0.31 parts of allyl methacrylate, 0.03 parts of t-butyl perpivalate, 0.03 parts of t-butyl per-2-ethylhexanoate, 0.1 parts of t-butyl perbenzoate and 0.077 parts of cumyl perneodecanoate. The polymerization is performed in flat chambers whose glass plates are spaced 23 mm, 30 mm and 50 mm apart respectively. For 23 mm the polymerization time is 80 hours at 37° C. and the postpolymerization time in the oven is 32 hours; for 30 mm spacing, 114 hours at 32° C., 10 hours at 32 to 38° C. and 24 hours at 38° C. as well as postpolymerization in the oven for 45 hours; for 50 mm spacing the polymerization time is 198 hours at 27° C., 24 hours at 27 to 37° C. and 24 hours at 37° C. Postpolymerization in the oven lasts for 57 hours. All plates exhibit regular structure and can be processed to foamed materials without difficulty.

Further examples are listed in tabular form in Table A.

TABLE A

Polymerization

Thickness

temperature

ΔT

Initiators

(mm)

(° C.)

(° C.)

DIPND:V77:V69:V73

0.083:0.03:0.04:0.07

23

38

2.0

0.078:0.03:0.04:0.07

23

38

1.4

0.09:0.03:0.04:0.07

23

38

2.3

0.09:0.03:0.04:0.07

30

35

3.4

0.09:0.03:0.04:0.07

50

29

2.3

ΔT denotes the maximum temperature difference between water bath and polymerization mixture during polymerization.

DIPND=1,4-di(2-neodecanoylperoxyisopropyl)benzene

TBPP=t-butyl perpivalate

TBPEH=t-butyl peroctoate

TBPB=t-butyl perbenzoate

The polymer plates obtained in this way have a uniform regular structure. During polymerization, which is controlled by a constant water-bath temperature (polymerization temperature), the temperature in the polymerizing mass also remains practically constant. The differences inside the polymerizing mass are only a few degrees, at most 3.4° C. The temperature during polymerization is monitored by a thermocouple inserted into the polymerizing mass. The slight temperature fluctuations are negligible, and are far removed from the temperature excursions that occur when the operation is performed with only one or two initiators and it is tried to control the reaction with an isothermal water bath. Under those conditions temperature excursions of 13° C. and more occur, whereby the polymerization becomes uncontrollable, accelerated polymerization occurs and plates are obtained which either are of low quality or must be scrapped.

It was further surprising that the inventive process can also be applied to the production of polymer plates or to the corresponding plate-shaped or sheet-shaped foamed materials that contain fillers. For example, plates containing standard fillers can be obtained. In a preferred embodiment of the invention, it is also possible to produce foamed materials which contain electrically conductive particles, especially carbon particles such as conductive carbon black, an example being Ketjenblack 600EC, a commercial product manufactured by Akzo Nobel Chemie. Besides carbon black, it is also possible to use carbon fibers as fillers either alone or in addition to other fillers.

Example 7

Production of polymer plates filled with carbon black

1680.00 g of carbon black (Ketjenblack 600EC) is dispersed for 50 minutes in 41901.18 g of methacrylic acid, 32656.08 g of methacrylonitrile, 2982.29 g of 2-propanol, 149.11 g of MgO and 1.4911 g of allyl methacrylate. The dissolved initiators are then stirred in and the polymerization solution is evacuated for 30 minutes. The polymerization solution is also stabilized with 50 ppm of quinone.

A second chamber is filled in the same way, except that dispersion lasts for 45 minutes and evacuation for 40 minutes. A third chamber is filled with the same composition, but dispersion is performed under vacuum for 25 minutes, after which evacuation is continued for a further 20 minutes. The polymerization was carried out at 34° C. for 73.25 hours in all three cases. Thereafter tempering was performed for 13 hours at 34 to 60° C., 3 hours at 60° C., 10 hours at 60 to 100° C., 5 hours at 100 to 115° C. and 3 hours at 115° C. The obtained polymer plates have flawless quality. The temperature fluctuations during polymerization are negligible.

TABLE 1

Half lives of organic peroxides

0.1 molar in benzene (unless otherwise indicated)

Activation

Temperature [° C.] for

INTEROX

energy

a half life of

No.

Code

Chemical name

[kJ/mol]

10 h

1 h

1 min

5)

1

ASCP

ACETYL CYCLOHEXANE SULFONYL PEROXIDE

124

31

46

75

2

DIPND

1,4-DI(2-NEODECANOYLPEROXYISOPROPYL)BENZENE

1)

114

37

54

85

3

CUPND

CUMYLPEROXY NEODECANOATE

115

38

55

90

4

*)

PEROXYDICARBONATE

124

41

57

90

5

IPPC

DIISOPROPYLPEROXY DICARBONATE

119

44

61

95

6

TAPND

Tert-AMYLPEROXY NEODECANOATE

113

44

62

100

7

TBPND

Tert-BUTYLPEROXY NEODECANOATE

121

47

64

100

8

TAPPI

Tert-AMYLPEROXY PIVALATE

121

53

71

110

9

DCLBP

DI(2,4-DICHLOROBENZOYL) PEROXIDE

121

54

72

110

10

TBPPI

Tert-BUTYLPEROXY PIVALATE

121

56

74

110

11

INP

DI(3,5,5-TRIMETHYLHEXANOYL) PEROXIDE

117

59

78

120

12

DP

DIDECANOYL PEROXIDE

126

62

80

120

13

LP

DILAUROYL PEROXIDE

126

62

80

120

14

DI(2-METHYLBENZOYL) PEROXIDE

119

62

81

120

15

DHPEH

2,5-DIMETHYL-2,5-DI(2-ETHYLHEXANOYLPEROXY)HEXANE

137

67

84

125

16

PMBP

DI(4-METHYLBENZOYL) PEROXIDE

125

70

89

130

17

BP

DIBENZOYL PEROXIDE

126

72

91

130

18

TAPEH

Tert-AMYLPEROXY 2-ETHYLHEXANOATE

126

72

91

130

19

TBPEH

Tert-BUTYLPEROXY 2-ETHYLHEXANOATE

135

74

92

130

20

Tert-BUTYLPEROXY ISOBUTYRATE

130

77

96

135

21

TBPM

Tert-BUTYLMONOPEROXY MALEATE

116

82

104

150

22

TMCH

1,1-DI(tert-BUTYLPEROXY)-3,3,5-TRIMETHYLCYCLOHEXANE

2)

143

95

114

155

23

CH

1,1-DI(tert-BUTYLPEROXY)CYCLOHEXANE

2)

138

97

117

160

24

Tert-BUTYLPEROXY ISOPROPYLCARBONATE

138

97

117

160

25

TBPIN

Tert-BUTYLPEROXY 3,5,5-TRIMETHYLHEXANOATE

147

100

119

160

26

DHPBZ

2,5-DIMETHYL-2,5-DI(BENZOYLPEROXY)HEXANE

147

100

119

160

27

TBP-EHC

Tert-BUTYLPEROXY (2-ETHYLHEXYL)CARBONATE

2)

128

100

122

175

28

Tert-BUTYLPEROXY ACETATE

149

102

121

160

29

TABP

Tert-AMYLPEROXY BENZOATE

2)

143

102

122

160

30

TBPB

Tert-BUTYLPEROXY BENZOATE

143

104

124

165

31

BU

2,2-DI(tert-BUTYLPEROXY)BUTANE

2)

143

104

124

165

32

NBV

n-BUTYL-4,4-DI(tert-BUTYLPEROXY) VALERATE

141

110

131

175

33

EBU

ETHYL-3,3-DI(tert-BUTYLPEROXY) BUTYRATE

3)

144

114

135

180

34

DCUP

DICUMYL PEROXIDE

152

116

136

175

35

BCUP

Tert-BUTYLCUMYL PEROXIDE

154

118

138

180

36

DTAP

DI(tert-AMYL) PEROXIDE

4)

129

118

142

190

37

DIPP

DI(tert-BUTYLPEROXYISOPROPYL)BENZENE

142

120

142

190

38

DHBP

2,5-DIMETHYL-2,5-DI(tert-BUTYLPEROXY)HEXANE

142

120

142

190

39

DTBP

DI(tert-BUTYL) PEROXIDE

152

125

146

190

40

DYBP

2,5-DIMETHYL-2,5-DI(tert-BUTYLPEROXY)HEX-3-YNE

154

128

149

195

41

HMCN

3,3,6,6,9,9-HEXAMETHYL-1,2,4,5-TETRAOXACYCLONONANE

2)

146

135

158

205

42

TBHP

Tert-BUTYL HYDROPEROXIDE

149

173

200

260

43

CC DFH

3,4-DIMETHYL-3,4-DIPHENYLHEXANE

150

182

210

270

44

CC DFB

2,3-DIMETHYL-2,3-DIPHENYLBUTANE

195

210

234

285

(Half lives in hours)

No.

Nr.

20°

30°

40°

50°

60°

70°

80°

90°

100°

110°

120°

130°

140°

150°

160°

170°

180°

190°

1

57

11

2.4

0.5

—

—

—

—

—

—

—

—

—

—

—

—

—

2

—

40

7.3

1.9

0.5

—

—

—

—

—

—

—

—

—

—

—

—

—

3

—

40

7.3

1.9

0.5

—

—

—

—

—

—

—

—

—

—

—

—

—

4

—

55

12

2.7

0.7

—

—

—

—

—

—

—

—

—

—

—

—

—

5

—

—

18

4.2

1.2

—

—

—

—

—

—

—

—

—

—

—

—

—

6

—

—

19

4.7

1.4

—

—

—

—

—

—

—

—

—

—

—

—

—

7

—

—

28

6.5

1.8

0.5

—

—

—

—

—

—

—

—

—

—

—

—

8

—

—

—

16

4.0

1.1

—

—

—

—

—

—

—

—

—

—

—

—

9

—

—

—

17

4.5

1.2

—

—

—

—

—

—

—

—

—

—

—

—

10

—

—

—

21

5.7

1.5

0.5

—

—

—

—

—

—

—

—

—

—

—

11

—

—

—

31

8.8

2.3

0.8

—

—

—

—

—

—

—

—

—

—

—

12

—

—

—

42

12

3.2

1.0

—

—

—

—

—

—

—

—

—

—

—

13

—

—

—

42

12

3.2

1.0

—

—

—

—

—

—

—

—

—

—

—

14

—

—

—

42

12

3.5

1.1

—

—

—

—

—

—

—

—

—

—

—

15

—

—

—

68

20

6.0

2.1

—

—

—

—

—

—

—

—

—

—

—

16

—

—

—

—

37

10

3.3

1.0

—

—

—

—

—

—

—

—

—

—

17

—

—

—

—

48

13

3.8

1.2

—

—

—

—

—

—

—

—

—

—

18

—

—

—

—

—

13

4.0

1.3

—

—

—

—

—

—

—

—

—

—

19

—

—

—

—

—

16

4.5

1.3

—

—

—

—

—

—

—

—

—

—

20

—

—

—

—

—

23

6.7

1.8

0.6

—

—

—

—

—

—

—

—

—

21

—

—

—

—

—

—

13

4.2

1.6

0.6

—

—

—

—

—

—

—

—

22

—

—

—

—

—

—

—

18

5.8

1.7

—

—

—

—

—

—

—

—

23

—

—

—

—

—

—

—

21

6.9

2.2

—

—

—

—

—

—

—

—

24

—

—

—

—

—

—

—

23

7.3

2.3

0.7

—

—

—

—

—

—

—

25

—

—

—

—

—

—

—

33

10

2.8

0.8

—

—

—

—

—

—

—

26

—

—

—

—

—

—

—

—

10

2.5

0.7

—

—

—

—

—

—

—

27

—

—

—

—

—

—

—

—

10

3.7

1.3

—

—

—

—

—

—

—

28

—

—

—

—

—

—

—

—

13

3.7

1.1

—

—

—

—

—

—

—

29

—

—

—

—

—

—

—

—

15

3.9

1.3

—

—

—

—

—

—

—

30

—

—

—

—

—

—

—

—

18

5.3

1.6

0.5

—

—

—

—

—

—

31

—

—

—

—

—

—

—

—

18

5.4

1.5

0.5

—

—

—

—

—

—

32

—

—

—

—

—

—

—

—

30

10

3

1.1

—

—

—

—

—

—

33

—

—

—

—

—

—

—

—

—

19

5.6

2.2

0.7

—

—

—

—

—

34

—

—

—

—

—

—

—

—

—

21

5.7

1.8

0.6

—

—

—

—

—

35

—

—

—

—

—

—

—

—

—

25

7.6

2.3

0.8

—

—

—

—

—

36

—

—

—

—

—

—

—

—

—

28

7.9

3.4

1.3

—

—

—

—

—

37

—

—

—

—

—

—

—

—

—

32

10

3.3

1.2

—

—

—

—

—

38

—

—

—

—

—

—

—

—

—

32

10

3.3

1.2

—

—

—

—

—

39

—

—

—

—

—

—

—

—

—

—

18

6.3

2.1

0.7

—

—

—

—

40

—

—

—

—

—

—

—

—

—

—

24

8.2

2.8

0.9

—

—

—

—

41

—

—

—

—

—

—

—

—

—

—

18

6.0

2.3

0.9

—

—

—

42

—

—

—

—

—

—

—

—

—

—

—

—

—

—

30

13

5.3

—

43

—

—

—

—

—

—

—

—

—

—

—

—

—

—

—

33

13

5.3

44

—

—

—

—

—

—

—

—

—

—

—

—

—

—

—

—

—

75

*)

EHPC Di(2-ethylhexyl) peroxydicarbonate

CEPC Dicetyl peroxydicarbonate

MYPC Dimyristyl peroxydicarbonate

CHPC Dicyclohexyl peroxydicarbonate

BCHPC Di(4-tert-butylcyclohexyl) peroxydicarbonate

1)

0.1 molar in toluene

2)

0.1 molar in isododecane

3)

0.1 molar in mineral oil

4)

0.1 molar in styrene

5)

extrapolated recommended values

TABLE 2

INTEROX

No.

Code

Chemical name

1

ASCP

ACETYL CYCLOHEXANE SULFONYL PEROXIDE

2

DIPND

1,4-DI(2-NEODECANOYLPEROXYISOPROPYL)BENZENE

3

CUPND

CUMYLPEROXY NEODECANOATE

4

PEROXYDICARBONATE

5

IPPC

DIISOPROPYLPEROXY DICARBONATE

6

TAPND

Tert-AMYLPEROXY NEODECANOATE

7

TBPND

Tert-BUTYLPEROXY NEODECANOATE

8

TAPPI

Tert-AMYLPEROXY PIVALATE

9

DCLBP

DI(2,4-DICHLOROBENZOYL) PEROXIDE

10

TBPPI

Tert-BUTYLPEROXY PIVALATE

11

INP

DI(3,5,5-TRIMETHYLHEXANOYL) PEROXIDE

12

DP

DIDECANOYL PEROXIDE

13

LP

DILAUROYL PEROXIDE

14

DI(2-METHYLBENZOYL) PEROXIDE

15

DHPEH

2,5-DIMETHYL-2,5-DI(2-ETHYLHEXANOYLPEROXY)HEXANE

16

PMBP

DI(4-METHYLBENZOYL) PEROXIDE

17

BP

DIBENZOYL PEROXIDE

18

TAPEH

Tert-AMYLPEROXY 2-ETHYLHEXANOATE

19

TBPEH

Tert-BUTYLPEROXY 2-ETHYLHEXANOATE

20

Tert-BUTYLPEROXY ISOBUTYRATE

21

TBPM

Tert-BUTYLMONOPEROXY MALEATE

22

TMCH

1,1-DI(tert-BUTYLPEROXY)-3,3,5-TRIMETHYLCYCLOHEXANE

23

CH

1,1-DI(tert-BUTYLPEROXY)CYCLOHEXANE

24

Tert-BUTYLPEROXY ISOPROPYLCARBONATE

25

TBPIN

Tert-BUTYLPEROXY 3,5,5-TRIMETHYLHEXANOATE

26

DHPBZ

2,5-DIMETHYL-2,5-DI(BENZOYLPEROXY)HEXANE

27

TBP-EHC

Tert-BUTYLPEROXY (2-ETHYLHEXYL)CARBONATE

28

Tert-BUTYLPEROXY ACETATE

29

TABP

Tert-AMYLPEROXY BENZOATE

30

TBPB

Tert-BUTYLPEROXY BENZOATE

31

BU

2,2-DI(tert-BUTYLPEROXY)BUTANE

32

NBV

n-BUTYL-4,4-DI(tert-BUTYLPEROXY) VALERATE

33

EBU

ETHYL-3,3-DI(tert-BUTYLPEROXY) BUTYRATE

34

DCUP

DICUMYL PEROXIDE

35

BCUP

Tert-BUTYLCUMYL PEROXIDE

36

DTAP

DI(tert-AMYL) PEROXIDE

37

DIPP

DI(tert-BUTYLPEROXYISOPROPYL)BENZENE

38

DHBP

2,5-DIMETHYL-2,5-DI(tert-BUTYLPEROXY)HEXANE

39

DTBP

DI(tert-BUTYL) PEROXIDE

40

DYBP

2,5-DIMETHYL-2,5-DI(tert-BUTYLPEROXY)HEX-3-YNE

41

HMCN

3,3,6,6,9,9-HEXAMETHYL-1,2,4,5-TETRAOXACYCLONONANE

42

TBHP

Tert-BUTYL HYDROPEROXIDE

43

CC DFH

3,4-DIMETHYL-3,4-DIPHENYLHEXANE

44

CC DFB

2,3-DIMETHYL-2,3-DIPHENYLBUTANE

TABLE 3

Chemical Name

Structural Formula

V-70

2,2′-Azobis(4-methoxy- 2,4-dimethylvaleronitrile)

M.W. 308.42

V-65

2,2′-Azobis(2,4-dimethyl- valeronitrile)

M.W. 248.37

V-60

2,2′-Azobisisobutyronitrile

M.W. 164.21

V-601

Dimethyl 2,2′-azobisisobutyrate

M.W. 230.26

V-59

2,2′-Azobis(2-methyl- butyronitrile)

M.W. 192.26

V-40

1,1′-Azobis(1-cyclo- hexanecarbonitrile)

M.W. 244.34

V-30

2-(Carbamoylazo)- isobutyronitrile

M.W. 140.14

VR-110

2,2′-Azobis(2,4,4-trimethyl- pentane)

M.W. 254.46

V-19

2-Phenylazo-2,4-dimethyl- 4-methoxyvaleronitrile

M.W. 245.32

VR-160

2,2′-Azobis(2-methylpropane)

M.W. 142.24

VA-044

2,2′-Azobis (N,N′-dimeth- yleneisobutyramidine) dihydrochloride

M.W. 323.27

V-50

2,2′-Azobis (2-amidino- propane) dihydrochloride

M.W. 271.19

VA-061

2,2′-Azobis (N,N′-dimeth- yleneisobutyramidine)

M.W. 250.35

V-501

4,4′-Azobis (4-cyano- pentanoic acid)

M.W. 280.28

VA-080

2,2′-Azobis{2-methyl-N- [1,1-bis(hydroxymethyl)- 2-hydroxyethyl]propionamide}

M.W. 408.45

VA-082

2,2′-Azobis{2-methyl-N- [1,1-bis(hydroxymethyl) ethyl] propionamide}

M.W. 376.45

VA-086

2,2′-Azobis [2-methyl-N- (2-hydroxyethyl) propionamide]

M.W. 288.35

VA-088

2,2′-Azobis(isobutyramide) dihydrate

M.W. 236.27

Wako Pure Chemical Industries, Ltd.

10 hour half-life

decomposition

Solubility at 20° C. (g/100 g solvent)

Appearance

Melting Range

temperature

Toluene

n-Hexane

Ethanol

Methanol

Water

V-70

White crystalline

50-96° C.

30° C. in toluene

3.3 (Benzene)

1 at 25° C.

—

2.1 at 25° C.

&Circlesolid;

powder

(Decomposition)

V-65

White crystals

45-70° C.

51° C. in toluene

72

4

20.5 at 25° C.

22

&Circlesolid;

V-60

White crystalline

100-103° C.

65° C. in toluene

7 at 25° C.

—

3 at 25° C.

7.5 at 25° C.

&Circlesolid;

powder

V-601

Pale yellow wax

22-28° C.

66° C. in toluene

◯

◯

◯

◯

&Circlesolid;

(Decomposition

point 85-87° C.)

V-59

White crystalline

55-57° C.

67° C. in toluene

◯

—

◯

◯

&Circlesolid;

powder

(Decomposition

point 84-87° C.)

V-40

White crystals

113-115° C.

88° C. in toluene

33 (Benzene)

0.9

—

3.2

&Circlesolid;

V-30

Pale yellow crystals

76-78° C.

104° C. in toluene

—

—

◯

◯

◯

VR-110

Pale yellow crystals

23-24° C.

110° C. in

◯

◯

◯

—

&Circlesolid;

or pale yellow liquid

diphenylether

V-19

Transparent

(Boiling point

122° C. in xylene

◯

—

◯

◯

&Circlesolid;

yellow liquid

149-150° C./1 mmHg)

VR-160

Pale yellow liquid

(Boiling point

160° C. gas phase

◯

◯

◯

◯

&Circlesolid;

109-110° C.)

VA-044

White to pale

188-193° C.

44° C. in water

&Circlesolid;

&Circlesolid;

0.02

1.6

35.2

yellow crystals

(Decomposition)

or crystalline powder

V-50

White or off-white

160-169° C.

56° C. in water

&Circlesolid;

&Circlesolid;

—

2.1

23.2

granular

(Decomposition)

VA-061

Pale yellow

115-125° C.

61° C. in methanol

&Circlesolid;

—

2.8

9.4

0.5

powder

(Decomposition)

V-501

White crystalline

120-123° C.

69° C. in water

&Circlesolid;

—

◯

—

1

powder

(Decomposition)

VA-080

Pale yellow

150-155° C.

80° C. in water

&Circlesolid;

&Circlesolid;

—

1.8

2.0

crystalline powder

(Decomposition)

VA-082

Pale yellow

156-161° C.

82° C. in water

&Circlesolid;

&Circlesolid;

—

5.1

0.6

crystalline powder

(Decomposition)

VA-086

Pale yellow

140-145° C.

86° C. in water

&Circlesolid;

&Circlesolid;

—

4.5

2.4

crystalline powder

(Decomposition)

VA-088

Pale yellow

88-92° C.

88° C. in water

&Circlesolid;

&Circlesolid;

3.6

9.6

0.8

crystalline powder

(Decomposition)

◯ Readily soluble

&Circlesolid; Insoluble

Number	Name	Date	Kind
4576971	Baumgartner et al.	Mar 1986	A
5698605	Krieg et al.	Dec 1997	A
5928459	Geyer et al.	Jul 1999	A

Method for producing block-shaped polymethacrylimide foamed materials

Information

Patent Number

Date Filed

Date Issued

Inventors

Original Assignees

Examiners

Agents

CPC

US Classifications

Field of Search

US

International Classifications

Abstract

Description

Claims

Priority Claims (1)

PCT Information

US Referenced Citations (3)

Foreign Referenced Citations (1)