TL;DR: MonoXantphos and monoSPANphos afforded the most active, stable and selective catalysts known to date under commercially relevant production conditions for 1-methoxyocta-2,7-diene, the precursor to oct-1-ene.
Abstract: Butadiene and methanol were telomerised in the presence of palladium catalysts with ligands containing 8-diphenylphosphinochromane-like substituents at phosphorus. MonoXantphos and monoSPANphos afforded the most active, stable and selective catalysts known to date under commercially relevant production conditions for 1-methoxyocta-2,7-diene, the precursor to oct-1-ene.
TL;DR: The process which uses carbon as a reducing agent will probably be a cheap method of extraction when completely developed since it employs the simple reaction: MgO+C+XA-Mg+CO.
Abstract: Magnesium, Its Manufacture and Alloys WILLIAM K. ZINSZER, Permanente Metals Corporation, Permanente, California Magnesium, although eighth in abundance among the elements, does not exist in the free state. It is found in abundance across the earth's surface in the form of magnesite, which is mainly magnesium carbonate and calcium carbonate; as brucite, the hydroxide of magnesium; as magnesium chloride in brines; as carnalite, a double salt of magnesium and potassium chlorides; as serpentine, magnesium silicate; and, in sea-water as a small percentage of magnesium chloride. It was first isolated by the Englishman, Sir Humphrey Davy, in 1860. As recently as the 1920's however, work with the metal had scarcely passed the laboratory stage. Due to the character of magnesium oxide and the salts of magnesium, various methods of reducing the metal have been developed. Each of the methods obviously has its distinct advantages and disadvantages; they may be classified as follows: electrolytic, carbo-thermic, and silo-thermic. The electrolytic process, developed in this country by the Dow Chemical Company, was initially developed by I. G. Farbenindustrie in Germany and improved by Magnesium Elektron, Ltd., in England. The Dow process, as it is referred to in this country, grew out of the development of a cheap raw material in the magnesium chloride liquor residue from the brine treatments designed to use this material at Midland, Michigan. Its reduction to an almost anhydrous condition using dry hydrogen chloride gas was discovered and a cell was then developed capable of electrolyzing the salt. At the Dow Freeport plant in Texas, magnesia is recovered from salt water using lime to precipitate the magnesia. This substance is then converted to hydrous magnesium chloride by the addition of hydrochloric acid; changed to the almost anhydrous condition and the resulting salt used as the electrolyte in the cell where further reduction to the metal takes place through electrolysis. The Basic Magnesium Company at Las Vegas, Nevada, uses the electrolytic process. The magnesite ore is calcined to a degree which leaves a highly reactive magnesium oxide. This oxide is pelletted with carbonaceous material selected to give a high degree of porosity, and fed into chlorinating furnaces in which the magnesium oxide is converted to absolutely anhydrous Mg C12, the electrolyte for the cells. The electric current melts and decomposes the salt in the presence of the carbonaceous material, liberating chlorine gas at the anode. The residue from the impurity in the ore is filtered and recirculated until the metal floats to the surface at the cathode where it is dipped out. The carbo-thermic process used by Permanente Metals Corporation at Permanente, California (also called the Hansgirg process) is one of the most widely discussed processes at the present time. The process which uses carbon as a reducing agent will probably be a cheap method of extraction when completely developed since it employs the simple reaction: MgO+C+XA-Mg+CO. This reaction is reversible and requires very special equipment to achieve the temperature of 2200? necessary to permit reduction toward the right. Very
TL;DR: The Dow Chemical Liquefacion Process uses a unique catalyst system, based on emulsion technology, which generates a highly active, effective expendable catalyst and eliminates the problems currently encountered with fixed or ebullated bed processes as discussed by the authors.
Abstract: The Dow Chemical Liquefacion Process uses a unique patented catalyst system, based on emulsion technology, which generates a highly active, effective expendable catalyst and eliminates the problems currently encountered with fixed or ebullated bed processes. Dow has successfully operated a 200 lb/day miniplant for over 600 hours. A summary of the distinguishing features of the Dow process are: (1) The unique use of emulsion technology to generate extremely small highly active catalyst particles which makes an expendable catalyst economically attractive. (2) Improved product composition which yields more higher valued products. (3) Use of hydroclones to provide partial solids removal from slurry makeup oil and to provide partial recycle of the catalyst to the reactor. (4) Use of a liquid--liquid extractor to produce an essentially solids-free, low sulfur product oil and high solids concentrate suitable as a gasifier feedstock. A simplified flow sheet of the Dow Coal Liquefaction Process is shown and a brief description of the process is given.
TL;DR: The Procon/Dow process for recovering pure carbon dioxide from flue gases was described in this paper, which reduced degradation and vaporization losses to between 2 lb and 4 lb per ton of carbon dioxide produced.
Abstract: This paper describes the Procon/Dow process for recovering pure carbon dioxide from flue gases. An amine solvent has been developed by Dow Chemical U.S.A., this reduces degradation and vaporization losses to between 2 lb and 4 lb per ton of carbon dioxide produced. However, the process will only work with flue gases from natural gas-fired boilers, because of problems with the acidic components found in other flue gases. The purity of the final product is claimed to be over 99.5%.
TL;DR: Two improved processes for making acrylate esters and some valuable intermediates have been developed by Dow Chemical as mentioned in this paper, which are part of a continuing d chemistry program at Dow that reflects the revaluation of petrochemicals and feedstocks.
Abstract: Two improved processes for making acrylate esters and some valuable intermediates have been developed by Dow Chemical. They are part of a continuing d chemistry program at Dow that reflects the revaluation of petrochemicals and feedstocks (C&EN, March 5, 1984, page 24). One of the processes is based on a discovery that organic carbonates may be used as esterifying agents in carbonylations. Specifically, the acrylate esters can be made by reacting a vinyl halide with carbon monoxide and an organic carbonate in the presence of a Group VIII catalyst. Some of the conventional means for producing acrylate esters include the use of alcohols or polyglycols as esterifying agents in homogeneous and heterogeneous systems, normally with Group VIII metal catalysts or complexes. An excess of the esterifying agent is normally employed either to prevent formation of free halogen or hydrohalogen, or to be halogen acceptors. In the first Dow process, the reactor is pressurized with carbon ...