公开(公告)号：US20140114099A1

公开(公告)日：2014-04-24

申请号：US14053634

申请日：2013-10-15

Applicant: BASF SE

Inventor： Steffen Tschirschwitz ,  Kathrin Wissel-Stoll ,  Jochen Bürkle ,  Albena Kostova ,  Markus Schmitt ,  Veronika Wloka ,  Stephan Deuerlein ,  Marco Bosch ,  Steffen Oehlenschläger ,  Michael Schreiber ,  Gauthier Luc Maurice Averlant ,  Joni Joni ,  Roman Prochazka ,  Martin Bock ,  Alois Kindler ,  Daniela Malkowsky ,  Katharina Spuhl ,  Stefan Bitterlich ,  Daniel Pfeiffer

IPC: C07C5/29

CPC classification number: C07C5/29 ,  C07C5/10 ,  C07C7/08 ,  C07C7/163 ,  C07C2521/04 ,  C07C2521/06 ,  C07C2521/08 ,  C07C2523/46 ,  C07C2523/745 ,  C07C2523/75 ,  C07C2523/755 ,  C07C2527/11 ,  C07C2527/1206 ,  C07C2527/1213 ,  C07C2527/125 ,  C07C2527/126 ,  C07C2527/135 ,  C07C2601/14 ,  C07C13/10 ,  C07C13/18

Abstract: The present invention relates to a process for preparing cyclohexane by isomerizing a hydrocarbon mixture (HM1) comprising methylcyclopentane (MCP) in the presence of a catalyst. The catalyst is preferably an acidic ionic liquid. The starting material used is a stream (S1) which originates from a steamcracking process. The hydrocarbon mixture (HM1) obtained from this stream (S1) in an apparatus for aromatics removal has a reduced aromatics content compared to stream (S1), and (HM1) may optionally also be (virtually) free of aromatics. Depending on the type and amount of the aromatics remaining in the hydrocarbon mixture (HM1), especially in the case that benzene is present, the isomerization may additionally be preceded by performance of a hydrogenation of (HM1). In addition, depending on the presence of other components of (HM1), further purification steps may optionally be performed prior to or after the isomerization or hydrogenation. High-purity (on-spec) cyclohexane is preferably isolated from the hydrocarbon mixture (HM2) obtained in the isomerization, the specifications being, for example, those applicable to the use of the cyclohexane for the preparation, known to those skilled in the art, of caprolactam.

Abstract translation: 本发明涉及通过在催化剂存在下异构化包含甲基环戊烷（MCP）的烃混合物（HM1）来制备环己烷的方法。 催化剂优选为酸性离子液体。 使用的起始材料是来自蒸汽裂化过程的流（S1）。 在与物流（S1）相比，用于除去芳烃的装置中从该料流（S1）获得的烃混合物（HM1）具有降低的芳族化合物含量，（HM1）也可任选地（实际上）不含芳族化合物。 取决于残留在烃混合物（HM1）中的芳族化合物的类型和量，特别是在存在苯的情况下，异构化可另外进行（HM1）的氢化。 此外，根据（HM1）的其它组分的存在，可以任选地在异构化或氢化之前或之后进行进一步的纯化步骤。 高纯度（特定）环己烷优选与在异构化中获得的烃混合物（HM2）分离，其规格是例如适用于本领域技术人员已知的用于制备环己烷的那些 的己内酰胺。

公开(公告)号：US20180273557A1

公开(公告)日：2018-09-27

申请号：US15763651

申请日：2016-09-30

Applicant: BASF SE

Inventor： Tobias Lang ,  Karl-Heinrich Schneider ,  Zoltan Baan ,  Philip Muelheims ,  Steffen Tschirschwitz ,  Sascha Shuxia Zhu

IPC: C07F9/22

CPC classification number: C07F9/224 ,  C07F9/242 ,  C07F9/2458 ,  C07F9/2466 ,  C07F9/2475

Abstract: Provided herein is a use of a high-boiling solvent in a mixture comprising a (thio)phosphoric acid derivative and a process including the addition of a high-boiling solvent to a mixture comprising a (thio)phosphoric acid derivative to recover the (thio)phosphoric acid from the mixture by an evaporation process.

公开(公告)号：US20170158575A1

公开(公告)日：2017-06-08

申请号：US14902181

申请日：2014-06-27

Applicant: BASF SE

Inventor： Karl-Heinrich Schneider ,  Claudia Klodwig ,  Gregor Pasda ,  Alexander Wissemeier ,  Daniella Lohe ,  Achim Reddig ,  Christian Miyagawa ,  Wolfram Zerulla ,  Steffen Tschirschwitz ,  Ralf-Thomas Rahn ,  Ansgar Gereon Altenhoff ,  Stephan Hüffer

IPC: C05G3/08 ,  C05G3/00 ,  C09D5/00 ,  C09D179/02 ,  C09K15/22 ,  C09K15/18 ,  C09K15/06 ,  C05C9/00 ,  C09K15/28

CPC classification number: C05G3/08 ,  C05C9/00 ,  C05C9/005 ,  C05C11/00 ,  C05G3/0029 ,  C05G3/0041 ,  C09D5/00 ,  C09D179/02 ,  C09K15/06 ,  C09K15/10 ,  C09K15/18 ,  C09K15/22 ,  C09K15/26 ,  C09K15/28 ,  C09K15/30

Abstract: An composition comprising: (A) a mixture comprising at least one (thio)phosphoric acid triamide according to the general formula (I) R1R2N—P(X)(NH2)2, wherein X is oxygen or sulfur; R1 is a C1 to C20 alkyl, C3 to C20 cycloalkyl, C6 to C20 aryl, or dialkylaminocarbonyl group; R2 is H, or R1 and R2 together with the nitrogen atom linking them define a 5- or 6-membered saturated or unsaturated heterocyclic radical, which optionally comprises 1 or 2 further heteroatoms selected from the group consisting of nitrogen, oxygen, and sulfur, and (C) at least one amine selected from the group consisting of (C1) a polymeric polyamine, and (C2) an amine containing not more than one amino group and at least three alkoxy- or hydroxy-substituted C2 to C12 alkyl groups R21, wherein at least one of the groups R21 is different to the other groups R21, and (C3) an amine containing not more than one amino group and at least two alkoxy- or hydroxy-substituted C2 to C12 alkyl groups R22, wherein at least one of the groups R22 bears the alkoxy or hydroxy substituent at a secondary or tertiary carbon atom and wherein at least one of the groups R22 is different to the other group(s) R22, and (C4) an amine containing at least one saturated or unsaturated C8 to C40 alkyl group R23, and (C5) a saturated or unsaturated heterocyclic amine which contains at least one oxygen atom as ring atom and which does not contain a further alkoxy group.

公开(公告)号：US20140114103A1

公开(公告)日：2014-04-24

申请号：US14053659

申请日：2013-10-15

Applicant: BASF SE

Inventor： Markus Schmitt ,  Katharina Spuhl ,  Jochen Bürkle ,  Stefan Bitterlich ,  Steffen Tschirschwitz ,  Michael Hübner ,  Pawel Czajka

IPC: C07C5/31 ,  C07C5/10

CPC classification number: C07C5/31 ,  C07C5/10 ,  C07C5/29 ,  C07C2523/755 ,  C07C2527/125 ,  C07C2601/14 ,  C07C13/18

Abstract: The present invention relates to a process for preparing cyclohexane from benzene and/or methylcyclopentane (MCP) by hydrogenation or isomerization. Prior to the cyclohexane preparation, the dimethylpentanes (DMP) are removed in a distillation apparatus (D1) from a hydrocarbon mixture (HM1) comprising not only benzene and/or MCP but also DMP. If cyclohexane is already present in the hydrocarbon mixture (HM1), this cyclohexane is first removed together with DMP from benzene and/or MCP. This cyclohexane already present can be separated again from DMP in a downstream distillation step and recycled into the process for cyclohexane preparation.

Abstract translation: 本发明涉及通过氢化或异构化由苯和/或甲基环戊烷（MCP）制备环己烷的方法。 在环己烷制备之前，在不仅包含苯和/或MCP而且还包含DMP的烃混合物（HM1）的蒸馏装置（D1）中除去二甲基戊烷（DMP）。 如果烃混合物（HM1）中已经存在环己烷，则首先从苯和/或MCP与DMP一起除去该环己烷。 已经存在的环己烷可以在下游蒸馏步骤中再次从DMP分离并再循环到环己烷制备方法中。

公开(公告)号：US20140018591A1

公开(公告)日：2014-01-16

申请号：US13937351

申请日：2013-07-09

Applicant: BASF SE

Inventor： Steffen Tschirschwitz ,  Joni Joni ,  Jochen Bürkle ,  Stefan Bitterlich ,  Daniel Pfeiffer ,  Michael Hübner ,  Nicole Holub

IPC: C07C5/29

CPC classification number: C07C5/29 ,  C07C2601/14 ,  C07C13/18

Abstract: The present invention relates to a chemical conversion process, preferably an isomerization process, for at least one hydrocarbon in the presence of an ionic liquid. The chemical conversion is performed in a dispersion, with dispersion of the hydrocarbon (phase (B)) in the ionic liquid (phase (A)) in the dispersion, the volume ratio of phase (A) to phase (B) being in the range from 2.5 to 4:1 [vol/vol].

Abstract translation: 本发明涉及在离子液体存在下至少一种烃的化学转化方法，优选异构化方法。 在分散体中进行化学转化，其中烃（相（B））在分散体中的离子液体（相（A））中分散，相（A）与相（B）的体积比在 范围为2.5至4：1 [vol / vol]。