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    • 6. 发明授权
    • Production of aliphatic esters
    • 生产脂肪族酯
    • US06399812B1
    • 2002-06-04
    • US09559339
    • 2000-04-27
    • Tsoung Y. YanJen-Ray Chang
    • Tsoung Y. YanJen-Ray Chang
    • C07C6902
    • C07C67/40C07C69/24C07C69/14
    • Aliphatic esters, R'COOR are produced by reacting the corresponding alcohol, ROH having carbon numbers of the alkyl groups, R′ and R, between 0 and 9 and 1 and 10, respectively, with molecular oxygen in the presence of a dual functional catalyst comprising metal on acidic solid support. In particular, the process is used advantageously for production of ethyl acetate by conversion of ethanol. The reaction mixture from the reactor is separated through azeotropic distillation to recover the ethyl acetate as product and the by-product, acetaldehyde and acetic acid which could be recycled for further reaction. The process is characterized by high conversion of ethanol, high selectivity and high yield for ethyl acetate and low waste stream generation. The preferred catalyst is Pd on zeolites which is active, selective, stable and regenerable.
    • 脂肪族酯R'COOR是通过在双官能催化剂存在下使相应的醇R 1和R 10分别与0分别为0和9分子之间的烷基,R 1和R 2分别与分子氧反应的醇ROH 在酸性固体载体上包含金属。 特别地,该方法有利地用于通过乙醇转化生产乙酸乙酯。 通过共沸蒸馏分离来自反应器的反应混合物以回收作为产物的乙酸乙酯和可再循环用于进一步反应的副产物乙醛和乙酸。 该方法的特点是乙醇转化率高,乙酸乙酯选择性高,产率高,废液产生量低。 优选的催化剂是Pd活性,选择性,稳定和可再生的沸石。
    • 8. 发明授权
    • Reclamation of HF and recovery of gasoline from acid-soluble oil by
cracking
    • 回收HF,通过开裂从酸溶性油中回收汽油
    • US5476983A
    • 1995-12-19
    • US285674
    • 1994-08-04
    • Tsoung Y. Yan
    • Tsoung Y. Yan
    • B01J27/32C07C2/62
    • C07C2/62B01J27/32C07C2527/1206Y02P20/584
    • The present invention provides a method for reclaiming HF and producing valuable gasoline blending components from the conjunct polymeric byproducts (acid soluble oil or ASO) formed as a byproduct of acid-catalyzed isoparaffin-olefin alkylation comprising the steps of:(a) reacting isoparaffin and olefin in the presence of a liquid acid alkylation catalyst to form alkylate and ASO byproduct;(b) separating alkylate, unreacted isoparaffin, and a majority of said liquid acid alkylation catalyst from said ASO;(c) reacting said separated ASO of step (b) under conditions of elevated temperature and pressure to convert the hydrocarbon portion of said ASO to gasoline boiling range hydrocarbons and to liberate HF.In a preferred embodiment, the ASO is pre-mixed with hydrogen or a hydrogen donor before reaction at elevated temperature and pressure. In a particularly preferred embodiment, the elevated temperature reaction is carried out in the presence of a catalyst such as activated carbon.
    • 本发明提供了一种回收HF的方法,由作为酸催化的异链烷烃 - 烷基烷基化副产物形成的结合的聚合副产物(酸溶性油或ASO)制备有价值的汽油调配成分的方法,包括以下步骤:(a)使异链烷烃和 烯烃在液态酸烷基化催化剂存在下形成烷基化物和ASO副产物; (b)从所述ASO分离烷基化物,未反应的异链烷烃和大部分所述液体酸烷基化催化剂; (c)使步骤(b)的所述分离的ASO在升高的温度和压力的条件下反应,以将所述ASO的烃部分转化为汽油沸程烃并释放HF。 在优选的实施方案中,ASO在升高的温度和压力下在反应之前与氢或氢供体预混合。 在特别优选的实施方案中,升高的温度反应在催化剂如活性炭的存在下进行。
    • 9. 发明授权
    • Regeneration of used stretford solution for recycle
    • 用于再生的二手拉斯福溶液再生
    • US5380442A
    • 1995-01-10
    • US154055
    • 1993-11-18
    • Tsoung Y. Yan
    • Tsoung Y. Yan
    • B01D53/14B01D53/52C02F1/38C02F1/72B01D9/02
    • B01D53/1425B01D53/52C02F1/38C02F1/725C02F2103/18
    • Waste materials are removed from Stretford solution in the form of sulfates by catalytic oxidation. The Stretford solution, which was used to treat sulfur contaminated gas streams is first regenerated by oxidation to restore the vanadium present to a pentavalent form. It is then passed to a reaction zone where it is contacted with a catalyst and an oxygen source. The catalyst comprises a porous solid substrate on which a metal or metal compound insoluble in Stretford solution is deposited. Waste materials, primarily thiosulfates, are thus oxidized to sulfates. The effluent of the reaction zone is then passed to a crystallizer, where the sulfates are precipitated out as crystals of Glauber's salt. The Glauber's salt is recovered as a product and the Stretford solution is recycled to a scrubber for the treatment of gas streams.
    • 废料通过催化氧化以硫酸盐的形式从Stretford溶液中除去。 用于处理含硫污染气流的Stretford溶液首先通过氧化再生,以使钒以五价形式存在。 然后将其送入反应区,在反应区中与催化剂和氧源接触。 催化剂包括多孔固体基质,其上沉积了不溶于Stretford溶液的金属或金属化合物。 废物,主要是硫代硫酸盐,因此被氧化成硫酸盐。 然后将反应区的流出物送入结晶器,其中硫酸盐作为芒硝的晶体析出。 将芒硝的盐作为产品回收,Stretford溶液再循环至洗涤器处理气流。