Disclosed are the use of fluorine substituted olefins, including tetra- and penta-fluoropropenes, in a variety of applications, including in methods of depositing catalyst on a solid support, methods of sterilizing articles, cleaning methods and compositions, methods of applying medicaments, fire extinguishing/suppression compositions and methods, flavor formulations, fragrance formulations and inflating agents.

Provided is a method for continuously producing a cyclic carbonate, by which generation of a glycol in a reaction for synthesizing a cyclic carbonate is suppressed, and a cyclic carbonate having a high purity can be efficiently obtained even by simple purification. A method for continuously producing a cyclic carbonate, including filling a catalyst in a fixed-bed tube reactor, and continuously feeding carbon dioxide and an epoxide to the fixed-bed tube reactor to thereby bringing the carbon dioxide and the epoxide into contact with the catalyst, while continuously withdrawing the reaction liquid in the fixed-bed tube reactor, wherein the method includes a pre-treatment step in which a pre-treatment liquid containing a cyclic carbonate is brought into contact with the catalyst before feeding the carbon dioxide and the epoxide to the fixed-bed tube reactor, and the generated glycol is removed out of the system.

Disclosed herein are embodiments of a process which generally includes contacting i) a monomer or mixture of monomers, ii) a haloaluminate ionic liquid, and iii) one or more halide components in a reaction zone, and oligomerizing the monomer or mixture of monomers in the reaction zone to form an oligomer product. The combination of the haloaluminate ionic liquid and halide component can constitute a catalyst system which is used in embodiments of the process to produce the oligomer product.

Fluorine-containing titanium oxidenano-silica composite particles comprising a condensate of a fluorine-containing alcohol and an alkoxysilane, and titanium oxide and nano-silica particles, wherein the fluorine-containing alcohol is represented by the general formula:

R.sub.FAOH[I]

(wherein R.sub.F is a perfluoroalkyl group having 6 or less carbon atoms, or a polyfluoroalkyl group, in which some of the fluorine atom or atoms of the perfluoroalkyl group are replaced by a hydrogen atom or atoms, and which contains a terminal perfluoroalkyl group having 6 or less carbon atoms and a perfluoroalkylene group having 6 or less carbon atoms; and A is an alkylene group having 1 to 6 carbon atoms). The fluorine-containing titanium oxidenano-silica composite particles do not have difficulty in handling as with hydrogen fluoride, can be produced by using a fluorine-containing alcohol, which can be easily handled, and can produce a product capable of suppressing a decrease in the function of the titanium oxide as a photocatalyst even when subjected to a high-temperature heat treatment.

A catalyst composition comprises an inert hydrocarbon solvent, having dissolved therein a titanate of the formula Ti(OR).sub.4 wherein each R is the same or different, and is a hydrocarbon residue, and an organic aluminum compound, wherein a molar ratio of the organic aluminum compound and any alkene present in the catalyst composition is greater than one.

A waste gas treatment equipment includes a reactor defining a waste gas reaction space, an induction heating pipe disposed in and dividing the waste gas reaction space into inner and outer spaces, a coil protector disposed in the outer space and surrounding the induction heating pipe, a flow guide tube inserted into the inner space through a bottom wall of the reactor, and a high frequency coil disposed in the coil protector. A catalyst barrel has a barrel body sleeved on a top portion of the flow guide tube, including an outer wall provided with a plurality of through holes, and defining a receiving space communicating with the through holes and for receiving a catalyst. A scraper mechanism is provided in the reactor for scraping dust or crystals attached to the inner wall surface of the flow guide tube and the outer wall of the barrel body.

Described are methods for preparing a deuterated aldehyde using N-heterocyclic carbene catalysts in a solvent comprising D.sub.2O. The methods may be used to convert a wide variety of aldehydes (e.g., aryl, alkyl, or alkenyl aldehydes) to C-1 deuterated aldehydes under mild reaction conditions without functionality manipulation.

A process for preparing valpromide of formula I and sodium valproate of formula II which comprises: cyanoacetate and 1-chloropropane are subjected to composite catalytic dipropylation in the presence of alkali to obtain 2-cyano-2-valproate of formula III; 2-cyano-2-valproate is hydrolyzed and deacidified to give propylvaleronitrile of formula V; propylvaleronitrile is alcoholized in the presence of acid to give valpromide of formula I and valproate ester of formula VI; and valproate ester is hydrolyzed in a sodium hydroxide solution to afford sodium valproate of formula II.