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    • 1. 发明申请
    • Hydroxymethylfurfural Reduction Methods and Methods of Producing Furandimethanol
    • 羟甲基糠醛还原方法和生产呋喃二甲醇的方法
    • US20070287845A1
    • 2007-12-13
    • US11760634
    • 2007-06-08
    • Michael LilgaRichard HallenTodd WerpyJames WhiteJohnathan HolladayJohn FryeAlan Zacher
    • Michael LilgaRichard HallenTodd WerpyJames WhiteJohnathan HolladayJohn FryeAlan Zacher
    • C07D307/02
    • C07D307/42C07D307/46
    • A method of reducing hydroxymethylfurfural (HMF) where a starting material containing HMF in a solvent comprising water is provided. H2 is provided into the reactor and the starting material is contacted with a catalyst containing at least one metal selected from Ni, Co, Cu, Pd, Pt, Ru, Ir, Re and Rh, at a temperature of less than or equal to 250° C. A method of hydrogenating HMF includes providing an aqueous solution containing HMF and fructose. H2 and a hydrogenation catalyst are provided. The HMF is selectively hydrogenated relative to the fructose at a temperature at or above 30° C. A method of producing tetrahydrofuran dimethanol (THFDM) includes providing a continuous flow reactor having first and second catalysts and providing a feed comprising HMF into the reactor. The feed is contacted with the first catalyst to produce furan dimethanol (FDM) which is contacted with the second catalyst to produce THFDM.
    • 提供一种还原羟甲基糠醛(HMF)的方法,其中含有HMF的原料在包含水的溶剂中。 H 2被提供到反应器中,起始材料与含有至少一种选自Ni,Co,Cu,Pd,Pt,Ru,Ir,Re和Rh的金属的催化剂接触, 温度小于或等于250℃。氢化HMF的方法包括提供含有HMF和果糖的水溶液。 H 2 H 2和氢化催化剂。 HMF在等于或高于30℃的温度下相对于果糖选择性地氢化。制备四氢呋喃二甲醇(THFDM)的方法包括提供具有第一和第二催化剂的连续流动反应器,并向反应器中提供包含HMF的进料。 进料与第一催化剂接触以产生与第二催化剂接触以产生THFDM的呋喃二甲醇(FDM)。
    • 2. 发明申请
    • Process for Producing Cyclic Compounds
    • 生产环状化合物的方法
    • US20070173643A1
    • 2007-07-26
    • US11688022
    • 2007-03-19
    • Todd WerpyJohn FryeJames WhiteJohnathan HolladayAlan Zacher
    • Todd WerpyJohn FryeJames WhiteJohnathan HolladayAlan Zacher
    • C07D207/267C07D223/10C07D205/02
    • C07D207/404
    • The invention includes methods of processing an initial di-carbonyl compound by conversion to a cyclic compound. The cyclic compound is reacted with an alkylating agent to form a derivative having an alkylated ring nitrogen. The invention encompasses a method of producing an N-alkyl product. Ammonia content of a solution is adjusted to produce a ratio of ammonia to di-carboxylate compound of from about 1:1 to about 1.5:1. An alkylating agent is added and the initial compound is alkylated and cyclized. The invention includes methods of making N-methyl pyrrolidinone (NMP). Aqueous ammonia and succinate is introduced into a vessel and ammonia is adjusted to provide a ratio of ammonia to succinate of less than 2:1. A methylating agent is reacted with succinate at a temperature of from greater than 100° C. to about 400° C. to produce N-methyl succinimide which is purified and hydrogenated to form NMP.
    • 本发明包括通过转化为环状化合物来处理初始二羰基化合物的方法。 环状化合物与烷基化剂反应形成具有烷基化环氮的衍生物。 本发明包括生产N-烷基产物的方法。 调节溶液的氨含量以产生约1:1至约1.5:1的氨与二羧酸酯化合物的比例。 加入烷基化剂并将该初始化合物烷基化并环化。 本发明包括制备N-甲基吡咯烷酮(NMP)的方法。 将氨水和琥珀酸钠引入容器中,并调节氨以提供小于2:1的氨与琥珀酸的比例。 甲基化剂与琥珀酸酯在大于100℃至约400℃的温度下反应,生成N-甲基琥珀酰亚胺,将其纯化并氢化形成NMP。
    • 6. 发明申请
    • Method of forming a dianhydrosugar alcohol
    • 形成二脱水糖醇的方法
    • US20070173652A1
    • 2007-07-26
    • US11341961
    • 2006-01-26
    • Johnathan HolladayJianli HuYong WangTodd WerpyXinjie Zhang
    • Johnathan HolladayJianli HuYong WangTodd WerpyXinjie Zhang
    • C07D311/22
    • C07D307/20C07D493/04Y02P20/127
    • The invention includes methods of producing dianhydrosugars. A polyol is reacted in the presence of a first catalyst to form a monocyclic sugar. The monocyclic sugar is transferred to a second reactor where it is converted to a dianhydrosugar alcohol in the presence of a second catalyst. The invention includes a process of forming isosorbide. An initial reaction is conducted at a first temperature in the presence of a solid acid catalyst. The initial reaction involves reacting sorbitol to produce 1,4-sorbitan, 3,6-sorbitan, 2,5-mannitan and 2,5-iditan. Utilizing a second temperature, the 1,4-sorbitan and 3,6-sorbitan are converted to isosorbide. The invention includes a method of purifying isosorbide from a mixture containing isosorbide and at least one additional component. A first distillation removes a first portion of the isosorbide from the mixture. A second distillation is then conducted at a higher temperature to remove a second portion of isosorbide from the mixture.
    • 本发明包括生产二脱水甘油糖的方法。 多元醇在第一催化剂存在下反应形成单环糖。 将单环糖转移到第二反应器中,在第二反应器中,在第二催化剂的存在下将其转化为二脱水甘油醇。 本发明包括形成异山梨醇的方法。 在固体酸催化剂存在下,在第一温度下进行初始反应。 初始反应包括使山梨醇反应生成1,4-脱水山梨糖醇,3,6-脱水山梨糖醇,2,5-甘露聚糖和2,5-己烷。 利用第二温度,将1,4-脱水山梨醇和3,6-脱水山梨醇转化为异山梨醇。 本发明包括从含有异山梨醇和至少一种另外的组分的混合物中纯化异山梨醇的方法。 第一蒸馏从混合物中除去第一部分的异山梨醇。 然后在较高温度下进行第二次蒸馏以从混合物中除去第二部分的异山梨醇。
    • 7. 发明申请
    • Two-stage dehydration of sugars
    • 糖两步脱水
    • US20070173651A1
    • 2007-07-26
    • US11341930
    • 2006-01-26
    • Johnathan HolladayJianli HuYong WangTodd Werpy
    • Johnathan HolladayJianli HuYong WangTodd Werpy
    • C07D311/22
    • C07D493/04
    • The invention includes methods for producing dianhydrosugar alcohol by providing an acid catalyst within a reactor and passing a starting material through the reactor at a first temperature. At least a portion of the staring material is converted to a monoanhydrosugar isomer during the passing through the column. The monoanhydrosugar is subjected to a second temperature which is greater than the first to produce a dianhydrosugar. The invention includes a method of producing isosorbide. An initial feed stream containing sorbitol is fed into a continuous reactor containing an acid catalyst at a temperature of less than 120° C. The residence time for the reactor is less than or equal to about 30 minutes. Sorbitol converted to 1,4-sorbitan in the continuous reactor is subsequently provided to a second reactor and is dehydrated at a temperature of at least 120° C. to produce isosorbide.
    • 本发明包括通过在反应器内提供酸催化剂并使原料在第一温度下通过反应器来生产二脱水甘油的方法。 在通过色谱柱期间,至少一部分起始物质被转化为单一脱氢葡萄糖异构体。 单糖酐经受大于第一温度的第二温度以产生二脱水糖。 本发明包括一种生产异山梨醇的方法。 含有山梨醇的初始进料流在小于120℃的温度下进料到含有酸催化剂的连续反应器中。反应器的停留时间小于或等于约30分钟。 随后将连续反应器中转化为1,4-脱水山梨醇的山梨糖醇提供给第二反应器,并在至少120℃的温度下脱水以制备异山梨醇。