专利号:US-2025051339-A1 优先权日:2021-12-15 标题:Methods for the synthesis of complement factor d inhibitors 发明人:HASHIMOTO AKIHIRO 权利人:ALEXION PHARMA INC 摘要:The present disclosure provides methods for the synthesis of complement factor D inhibitors and intermediates thereof. The methods involve subjecting an intermediate in the synthesis of a complement factor D inhibitor to a t-butyl ester deprotection reaction using a weak base.
专利号:US-6540970-B1 优先权日:1999-11-18 标题:Method for the synthesis of molecular sieves 发明人:STROHMAIER KARL G; VAUGHAN DAVID E W 权利人:EXXON MOBIL CHEM PATENTS INC 摘要:The present invention provides a method for the synthesis of MeAPO molecular sieves which includes the following steps: providing a source of alumina, a source of phosphorus, water, and a template suitable for forming a MeAPO molecular sieve; providing a source of metal (Me) including metal particles, the metal particles measuring, in their largest dimension, equal to or less than five nanometers; providing a water soluble organic solvent capable of solubilizing the source of metal; forming a synthesis mixture from the source of alumina, the source of phosphorus, the water, the template, the source of metal, and the solvent; and forming a MeAPO molecular sieve from the synthesis mixture.
专利号:US-4902817-A 优先权日:1987-09-17 标 题 :Process for the synthesis of alpha n alkylated amino acids and esters thereof, application to the synthesis of carboxyalkyl dipeptides 发明人:VINCENT MICHEL; BALIARDA JEAN; MARCHAND BERNARD; REMOND GEORGES 权利人:ADIR 摘要:Stereoselective process for the industrial synthesis of compounds of formula (I): ##STR1## where R 1 is linear or branched lower alkyl with 1 to 6 carbon atoms, n R 2 is a linear or branched lower alkyl with 1 to 4 carbon atoms, n employing inexpensive starting materials and obtaining optimum yields. n Application to the synthesis of carboxyalkyl dipeptides.
专利号:US-9040739-B2 优先权日:2012-06-18 标题 :Catalyst and method for synthesis of lactic acid and its derivatives 发明人:ZHOU XIAOPING; BI RUI 权利人:ZHOU XIAOPING; BI RUI; MICROVAST POWER SYSTEMS CO LTD 摘要:A catalyst for synthesis of lactic acid and it derivatives is provided. The catalyst includes SnY2.mH 2 O and at least one of NH 4 X or quaternary ammonium salts, wherein X and Y are selected from F—, Cl—, Br—, I—, CH 3 SO 3 —, C 6 H 5 SO 3 —, CH 3 C 6 H 4 SO 3 — or CN—, m represents an integer of 1 to 15. A method for synthesis of lactic acid and it derivatives with the above catalyst is also provided. By using the above catalyst and method, it is capable of converting carbohydrate-containing raw material to lactic acid and its derivatives directly in a more efficient and economical way.
专利号:US-4174345-A 优先权日:1978-08-01 标题:Synthesis of steroids 发明人:KAISER EMIL T 权利人:KAISER EMIL T 摘要:In the synthesis of sterols wherein methoxyethoxymethyl groups in an ether linkage are attached to the nucleus of the sterol to protect the sterol nucleus during other steps of the synthesis and the sterols are thereafter treated to remove the methoxyethoxymethyl groups and set free the hydroxyl groups, the improvement in which the sterols being treated with zinc bromide are held in a methylene chloride solution containing a small amount of an aliphatic alcohol having from 1 to 6 carbon atoms.
专利号:US-4477594-A 优先权日:1982-12-16 标题 :Process for the synthesis of aliphatic alcohol-containing mixtures 发明人:GREENE MARVIN I; GELBEIN ABRAHAM P 权利人:CHEM SYSTEMS 摘要:A process for the synthesis of mixtures which include saturated aliphatic alcohols is disclosed. In the first step of the process, the first catalyst activation stage, a catalyst, which comprises the oxides of copper, zinc, aluminum, potassium and one or two additional metals selected from the group consisting of chromium, magnesium, cerium, cobalt, thorium and lanthanum, is partially activated. In this step, a reducing gas stream, which includes hydrogen and at least one inert gas, flows past the catalyst at a space velocity of up to 5,000 liters (STP) per hour, per kilogram of catalyst. The partially activated catalyst is then subjected to the second step of the process, second-stage catalyst activation. In this step, the catalyst is contacted by an activation gas stream comprising hydrogen and carbon monoxide present in a volume ratio of 0.5:1 and 4:1, respectively, at a temperature of 200 DEG to 450 DEG C. and a pressure of between 35 and 200 atmospheres. The activation gas flows at a space velocity of from 1,000 to 20,000 liters (STP) per hour, per kilogram of catalyst. Second-stage activation continues until the catalyst is contacted with at least 500,000 liters (STP) of activation gas per kilogram of catalyst. The fully activated catalyst, in the third step of the process, contacts a synthesis gas stream comprising hydrogen and carbon monoxide.