The present invention relates to a vinylidene chloride interpolymer. Specifically, the present invention relates to pellets of a vinylidene chloride interpolymer which pellets possess improved extrudability.

Vinylidene chloride interpolymers are well- known in the prior art. In the past, vinylidene chloride interpolymers have been produced by an emulsion or suspension polymerization process. Both the emulsion and suspension polymerization processes produce an aqueous dispersion of polymer particles having a relatively small particle diameter. The polymer particles are recovered from the aqueous dispersion by drying or other means for removing a majority of the aqueous phase. In the past, the practice has been to extrude the vinylidene chloride interpolymer directly from the form in which it is recovered.

In some instances, it is desirable to form the vinylidene chloride interpolymer into pellets prior to extrusion. Unfortunately, it has been found that

such pellets are not easily extrudable. Attempts to extrude vinylidene chloride interpolymer pellets on certain extrusion equipment have proven unsatisfactory due to variations in extrusion rate, torque within the extruder, and pressure within the extruder. Unsatisfactory results are particularly evident during start-up of the extrusion process. It is believed that the variations in extrusion rate, torque, and pressure are a result of poor forwarding of the vinylidene chloride interpolymer within the extruder.

It is desirable to produce a vinylidene chloride interpolymer pellet which pellet is capable of being extruded without exhibiting variations in extrusion rate, torque within the extruder, and pressure within the extruder. It is to this goal that the present invention is directed.

The present invention concerns a process for improving the extrudability of a vinylidene chloride interpolymer, said vinylidene chloride interpolymer being in the form of pellets, said vinylidene chloride interpolymer pellets displaying a first endotherm, as determined by differential scanning calorimetry according to American Society for Testing and Materials Test Method 0-3 17, below 75°C, wherein the process comprises: exposing said vinylidene chloride interpolymer to a temperature of at least 55°C for a length of time sufficient to raise said first endotherm to 75°C or above.

Additionally, the present invention concerns pellets formed by the above described process.

Vinylidene chloride interpolymers suitable for use in the present invention are those vinylidene chloride interpolymers formed from vinylidene chloride and an amount of one or more monoethylenically unsaturated monomers copolymerizable with vinylidene chloride.

The vinylidene chloride interpolymers have polymerized therein vinylidene chloride in an amount of from 40 to 98 weight percent, beneficially from 50 to 96 weight percent, and desirably from 60 to 94 weight percent, based on total weight of the vinylidene chloride interpolymer.

The vinylidene chloride interpolymer comprises one or more monoethylenically unsaturated monomer copolymerizable with vinylidene chloride. The amount of monoethylenically unsaturated monomer is suitably from 60 to 2 weight percent, beneficially from 50 to 4 weight percent, and desirably from 40 to 6 weight percent, based on total weight of the vinylidene chloride interpolymer.

Monoethylenically unsaturated monomers suitable for use in the present invention include vinyl chloride, alkyl acrylates, alkyl methacrylates, acrylic acid, methacrylic acid, itaconic acid, acrylonitrile, and methacrylonitrile. The ethylenically unsaturated monomers are desirably selected from vinyl chloride, alkyl acrylates, and alkyl methacrylates, the alkyl acrylates and alkyl methacrylates having from 1 to 8 carbon atoms per alkyl group. The alkyl acrylates and alkyl methacrylates preferably have from 1 to 4 carbon atoms per alkyl group. The alkyl acrylates and alkyl methacrylates are most preferably selected from

methylacrylates, ethylacrylates, and methylmethacrylates.

Methods of forming the vinylidene chloride interpolymers suitable for use in the present invention are well-known in the prior art. The vinylidene chloride interpolymer is generally formed through an emulsion or suspension polymerization process. Exemplary of such processes are U.S. Patents 2,558,728; 3,007,903; 3,642,743; and 3,879,359; and the methods described by R. A. essling, in Polyvinylidene Chloride, Gordon and Breach Science Publishers, New York, 1977, Chapter 3. Typically, the monomeric materials are emulsified or suspended in an aqueous phase. The aqueous phase contains a polymerization initiator and a surface active agent capable of emulsifying or suspending the monomeric materials in the aqueous phase. The polymerization of the monomeric materials is usually carried out with heating and agitation. After polymerization is complete, the resulting suspension or emulsion of vinylidene chloride interpolymer has a majority of the aqueous phase removed.

The vinylidene chloride interpolymer which results from suspension or emulsion polymerization of the vinylidene chloride interpolymer is then pelletized. Methods of forming the vinylidene chloride interpolymer into pellets are well-known to those skilled in the art. Any method capable of forming the vinylidene chloride interpolymer into pellets is suitable for use in the present invention. For the purposes of this application, the terms "pellet" or

"pellets" refer to particles typically having a minimum cross-sectional dimension of at most 1/32 inch (0.8

mm), beneficially of at least 1/16 inch (1.6 mm), and preferably of at least 1/8 inch (3.2 mm). Said pellets suitably have a maximum cross-sectional dimension of at most 1/2' inch (13 mm), beneficially of at least 3/8 inch (8.5 mm), and preferably of at least 1/4 inch (6.5 mm) . Exemplary of a method suitable for use in forming the pellets of vinylidene chloride interpolymer are extrusion through a strand die and pelletization by chopping the extruded strand into pellets.

The vinylidene chloride interpolymer pellets of the present invention may contain a number of additives well-known to those skilled in the art. Exemplary of additives which may be incorporated in the vinylidene chloride interpolymer pellets of the present invention are plasticizers, heat stabilizers light stabilizers, pigments, processing aids, lubricants, and ^* the like.

Each of these additives is known and several types of each are commercially available.

The pellets of vinylidene chloride interpolymer display a first endotherm, as determined by differential scanning calorimetry according to American Society for Testing and Materials Test Method D-3417, below 75°C. By the term "first endotherm" is meant the endotherm revealed through differential scanning calorimetry which occurs at the lowest temperature. Additionally, in order to be considered an endotherm within the scope of the term as used in the present invention, it is necessary that the endotherm revealed through differential scanning calorimetry represent a morphological change consuming more than 0.3 Joules of energy per gram of polymer.

The differential scanning calorimetry used in the present invention to determine the location of the first endotherm is practiced in accordance with American Society for Testing and Materials Test Method D-3417 as approved for use in 1975.

Pellets of vinylidene chloride interpolymer displaying a first endotherm below 75°C have been found to be difficult to extrude. It is believed that the 10 difficulty in extrusion is related to poor forwarding of the vinylidene chloride interpolymer pellets within the extruder.

Applicants have discovered that exposing the 15 pellets of vinylidene chloride interpolymer to a temperature above 55°C for a length of time sufficient to raise said first endotherm to 75°C or above results in vinylidene chloride interpolymer pellets which extrude well. 0

The vinylidene chloride interpolymer pellets are exposed to a temperature of at least 55°C, beneficially the vinylidene interpolymer pellets are exposed to a temperature between 70°C and 100°C.

25 Preferably, the vinylidene chloride interpolymer pellets are exposed to a temperature between 85°C and 95°C. The vinylidene chloride interpolymer pellets are exposed to the elevated temperatures for a length of

30 time sufficient to raise the first endotherm to 75°C or above; beneficially to 80°C or above and desirably to 90°C or above.

The length of time for which the vinylidene ■ ₃ ,- chloride interpolymer pellets must be exposed to a temperature of at least 55°C depends, in part, upon the

temperature chosen. For example, when the pellets are exposed to a temperature of 55°C, exposure must continue for a period of 26 hours to raise the first. endotherm above 75°C. However, when the pellets are exposed to a temperature of 90°C, exposure need only continue for a period of about 1 minute.

In any event, the temperature of exposure and time of exposure are chosen so that the vinylidene chloride interpolymer does not degrade to an unacceptable level.

In one preferred embodiment of the present invention, the vinylidene chloride interpolymers are exposed to a temperature of 90°C for a length of time of one minute. This temperature and time combination has been found sufficient to raise the first endotherm of a vinylidene chloride interpolymer pellet comprising 85 weight percent vinylidene chloride and 15 weight percent vinyl chloride based on total vinylidene chloride interpolymer weight, to 90°C.

The optimum combination of temperature and time for a particular vinylidene chloride interpolymer pellet can be easily determined through a series of simple experiments. Moreover, it appears that once the minimum time and temperature combination to raise the first endotherm to 75°C or above has been reached, continued exposure of the vinylidene chloride interpolymer pellets to the elevated temperature does not appear to harm the vinylidene chloride interpolymer pellets so long as the temperature is not raised to a point such that an unacceptable amount of degradation occurs in the vinylidene chloride interpolymer pellet.

The vinylidene chloride interpolymer pellets processed according to the present invention can be extruded or otherwise processed into films or a variety of other articles.

The present invention is illustrated in further detail by the following examples. The examples are for purposes of illustration only, and are not to be construed as limiting the scope of the present

10 invention. All parts and percentages are by weight unless otherwise specifically noted.

Example 1

A vinylidene chloride Interpolymer is formed

15 through a suspension polymerization process. The vinylidene chloride interpolymer is formed from a monomer mixture comprising 80 weight percent vinylidene chloride and 20 weight percent vinyl chloride based on total monomer mixture weight. The vinylidene chloride

20 interpolymer powder produced from the suspension polymerization process is pelletized by extrusion through a strand die and subsequently chopping the strand into pellets. The pellets have an average

_2c length of 0.130 inch (3«3 mm) and an average diameter of 0.145 inch (3.7 mm). The vinylidene chloride interpolymer pellets thus formed exhibits a first endotherm at 60°C.

■a- The vinylidene chloride interpolymer pellets are exposed to a temperature of 100°C for 21 hours. After exposure to the elevated temperature, the vinylidene chloride interpolymer pellets exhibit a first endotherm at 92°C. The vinylidene chloride

35 interpolymer pellets thus treated are extruded in a 2.5 inch (6.5 cm) extruder under normal extrusion

conditions for a vinylidene chloride interpolymer. The vinylidene chloride interpolymer pellets are found to extrude well and maintain a relatively constant rate, torque, and pressure.

Example 2

The vinylidene chloride interpolymer pellets produced as described above in the first paragraph of

Example 1 are exposed to a temperature of 100°C for 1 minute. The vinylidene chloride interpolymer pellets thus treated exhibit a first endotherm of greater than

90°C. The vinylidene chloride interpolymer pellets are found to extrude well, maintaining a relatively constant rate, torque, and pressure.