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    • 4. 发明申请
    • Method for producing chlorine from hydrochloric from hydrochloric aid
    • 从盐酸辅助的盐酸生产氯的方法
    • US20060099138A1
    • 2006-05-11
    • US10532725
    • 2003-10-27
    • Christian WalsdorffMartin FieneChristian KuhrsEckhard StroeferKlaus Harth
    • Christian WalsdorffMartin FieneChristian KuhrsEckhard StroeferKlaus Harth
    • C01B7/00
    • C01B7/0718C01B7/04C01B7/0743C07C263/10C07C265/14C07C265/06
    • Process for preparing chlorine from hydrochloric acid, which comprises the steps: a) providing a hydrochloric acid feed stream I; b) providing a hydrochloric acid recycle stream II; c) separating off a hydrogen chloride stream IV from the hydrochloric acid feed stream I and the hydrochloric acid recycle stream II in a distillation step; d) feeding the hydrogen chloride stream IV, an oxygen-containing steam V and, if desired, an oxygen-containing recycle stream Va into an oxidation zone and oxidizing hydrogen chloride to chlorine in the presence of a catalyst to give a product gas stream VI comprising chlorine, unreacted oxygen, unreacted hydrogen chloride and water vapor; e) separating off hydrogen chloride and water from the product gas stream VI in an absorption step to give a gas stream VII and the hydrochloric acid recycle stream II; f) if desired, drying the gas stream VII; g) separating off an oxygen-containing stream from the gas stream VII and, if desired, recirculating at least part of this as oxygen-containing recycle stream Va to the oxidation zone, leaving a chlorine-containing product stream VIII; h) if desired, further purifying the chlorine-containing product stream VIII.
    • 从盐酸制备氯的方法,其包括以下步骤:a)提供盐酸进料流I; b)提供盐酸循环流II; c)在蒸馏步骤中,从盐酸进料流I和盐酸循环流II中分离出氯化氢料流IV; d)将氯化氢流IV,含氧蒸汽V以及如果需要的话将含氧再循环流Va加入氧化区,并在催化剂存在下将氯化氢氧化成氯,得到产物气流VI 包括氯,未反应的氧,未反应的氯化氢和水蒸气; e)在吸收步骤中从产物气流VI中分离氯化氢和水,得到气流VII和盐酸再循环流II; f)如果需要,干燥气流VII; g)从气流VII中分离含氧物流,如果需要,将其至少部分再循环为含氧再循环流Va至氧化区,留下含氯产物流VIII; h)如果需要,进一步纯化含氯产物流VIII。
    • 8. 发明授权
    • Method for the production of butadiene from n-butane
    • 从正丁烷生产丁二烯的方法
    • US07034195B2
    • 2006-04-25
    • US10516920
    • 2003-07-10
    • Götz-Peter SchindlerChristian WalsdorffKlaus HarthHartmut Hibst
    • Götz-Peter SchindlerChristian WalsdorffKlaus HarthHartmut Hibst
    • C07C5/333
    • C07C5/3335C07C5/3337C07C11/167
    • The invention relates to a process for preparing butadiene from n-butane comprising the steps (A) providing an n-butane-containing feed gas stream, (B) feeding the n-butane-containing feed gas stream into a first dehydrogenation zone and nonoxidatively catalytically dehydrogenating n-butane to 1-butene, 2-butene and optionally butadiene to obtain a first product gas stream comprising n-butane, 1-butene and 2-butene, with or without butadiene and secondary components, (C) feeding the first product gas stream comprising n-butane, 1-butene and 2-butene, with or without butadiene and secondary components, into a second dehydrogenation zone and oxidatively dehydrogenating 1-butene and 2-butene to butadiene to give a second product gas stream comprising butadiene, n-butane and steam, with or without secondary components, (D) recovering butadiene from the second product gas stream.
    • 本发明涉及一种从正丁烷制备丁二烯的方法,包括步骤(A)提供含正丁烷的原料气流,(B)将含正丁烷的进料气流进料到第一脱氢区和非氧化反应 将正丁烷催化脱氢为1-丁烯,2-丁烯和任选的丁二烯以获得含有或不具有丁二烯和二级组分的正丁烷,1-丁烯和2-丁烯的第一产物气流,(C) 将包含或不具有丁二烯和次要组分的正丁烷,1-丁烯和2-丁烯的产物气流转化为第二脱氢区并将1-丁烯和2-丁烯氧化脱氢成丁二烯,得到包含丁二烯的第二产物气流 正丁烷和蒸汽,具有或没有二级组分,(D)从第二产物气流回收丁二烯。
    • 10. 发明申请
    • Method for the production of butadiene from n-butane
    • 从正丁烷生产丁二烯的方法
    • US20050171311A1
    • 2005-08-04
    • US10516920
    • 2003-07-10
    • Goetz-Peter SchindlerChristian WalsdorffKlaus HarthHartmut Hibst
    • Goetz-Peter SchindlerChristian WalsdorffKlaus HarthHartmut Hibst
    • B01J23/62C07B61/00C07C5/333C07C11/167C08F36/00
    • C07C5/3335C07C5/3337C07C11/167
    • The invention relates to a process for preparing butadiene from n-butane comprising the steps (A) providing an n-butane-containing feed gas stream, (B) feeding the n-butane-containing feed gas stream into a first dehydrogenation zone and nonoxidatively catalytically dehydrogenating n-butane to 1-butene, 2-butene and optionally butadiene to obtain a first product gas stream comprising n-butane, 1-butene and 2-butene, with or without butadiene and secondary components, (C) feeding the first product gas stream comprising n-butane, 1-butene and 2-butene, with or without butadiene and secondary components, into a second dehydrogenation zone and oxidatively dehydrogenating 1-butene and 2-butene to butadiene to give a second product gas stream comprising butadiene, n-butane and steam, with or without secondary components, (D) recovering butadiene from the second product gas stream.
    • 本发明涉及一种从正丁烷制备丁二烯的方法,包括步骤(A)提供含正丁烷的原料气流,(B)将含正丁烷的进料气流进料到第一脱氢区和非氧化反应 将正丁烷催化脱氢为1-丁烯,2-丁烯和任选的丁二烯以获得含有或不具有丁二烯和二级组分的正丁烷,1-丁烯和2-丁烯的第一产物气流,(C) 将包含或不具有丁二烯和次要组分的正丁烷,1-丁烯和2-丁烯的产物气流转化为第二脱氢区并将1-丁烯和2-丁烯氧化脱氢成丁二烯,得到包含丁二烯的第二产物气流 正丁烷和蒸汽,具有或没有二级组分,(D)从第二产物气流回收丁二烯。