What is claimed is:
1. A method for generating a link means in a file and updating text in the file on a computer network, wherein a provider computer and a user computer are in communication via the computer network, and wherein the user computer is capable of accessing the file, comprising:
selecting key words and placing each key word a key word list;
creating an association between each key word and predefined data;
creating a linking means between the key word and the predefined data, wherein the user can access the predefined data via the linking means.
2. A system for generating a link means in a file and updating text in that file on a computer network, wherein a provider computer and a user computer are in communication via the computer network, and wherein the user computer is capable of accessing the file, comprising:
a database for storing selected key words;
a means for creating an association between each key word and predefined data;
a means for creating a linking means between the key word and the predefined data, wherein the user can access the predefined data via the linking means.
The claims below are in addition to those above.
All refrences to claim(s) which appear below refer to the numbering after this setence.
1. A process for producing a liquid non-aqueous dispersion having a copolymer dispersed in a silicone oil, which comprises copolymerizing (A) 1 to 20% by weight of at least one radical polymerizable macromonomer containing dimethyl polysiloxane, the macromonomer (A) being represented by the formula (1):
(wherein X represents a radical polymerizable group, n is an integer of 1 to 10, and m is an integer of 3 to 300), and (B) 99 to 80% by weight of at least one radical copolymerizable monomer with said macromonomer (A), the monomer (B) comprising at least one (meth)acrylate monomer and optionally at least one vinyl monomer, by subjecting said monomers to one-step polymerization in a silicone oil in the presence of a radical polymerization initiator without a dispersion stabilizer.
2. The process according to claim 1, wherein the amount of the radical polymerization initiator is 0.01 to 5% by weight based on the whole amount of the monomers.