Linde Aktiengesellschaft

Saudi Basic Industries Corporation

Linde Gmbh

Basf Se Corporation

Basf Se (isenbruck Bösl Hörschler Llp)

Müller, Bernd H.

Anton Wellenhofer

Heinz Bölt

Wolfgang Müller

Anina Wöhl

Florian Winkler

Mohammed Hassan Al-Hazmi

Fuad Mosa

Vugar O Aliyev

Normen Peulecke

Uwe Rosenthal

Peter M Fritz

Mathieu Zellhuber

Ulrike Wenning

Bernd H Müller

Jan Pablo Josch

Hendrik Reyneke

Christine Toegel

Marko Hapke

Helmut Fritz

Andreas Meiswinkel

Martin Schubert

Heinrich Laib

Heinz Boelt

Karl-Heinz Hofmann

Eric Jenne

Clara Delhomme-Neudecker

Andrey Shustov

Reiner Jacob

Heinz-Jürgen Kühn

Martin Hofstätter

Kiara Aenne Kochendörfer

Robert Stegemann

Christian Ziegler

Christian Walsdorff

Marco Harff

Hans-Jörg Zander

Anina Woehl

Ragavendra Prasad Balegedde Ramachandran

Shahid Azam

Regina Benfer

Wolfgang Peter Mueller

Heinz Posselt

Steffen Rissel

Georg Kiese

Peter Reiser

Bernd H Mueller

Jens Aengenheister

Jürgen Feigl

Shehzada Khurram

Philipp Grüne

Richard Schneider

Sultan Eid Al-Otaibi

Abdullah Al-Qahtani

Abduljelil Iliyas

Michael Baus

Nicole Schödel

Franz Beran

Syriac Palackal

Oliver Hammen

Harald Ranke

Wolfgang Schmehl

Karl Heinz Hofmann

Hans Jorg Zander

Hans-Jorg Zander

Mohammed Zahoor

Carsten Taube

Georgios Karanikoulis

Michael Rothe

Claudia Mossbacher

Florian Hairer

Ekaterina Ananieva

Stephan Deublein

Jörg Zander

Rainer Rahm

Daniela Lauchner

Heinz-Dieter Obermeyer

Volker Jeromin

Christian Lang

André Biegner

Robert Birk

Ayed Al-Ayed

Celine Pichler

Philipp Gruene

Mariyana Chalakova

Wibke Korn

Eva Müller

Stefan Felbinger

Kathrin Wellenhofer

Petya Toneva

Harald Zenz

Christian Zach

Niklas Fleischmann

Martin Gembala

Andreas Wolf

Marius Dillig

Ole Müller-thorwart

Christian Fruhmann

Robert Herzog

A reactor includes a reactor vessel and one or more reaction tubes A number of tube sections of the one or more reaction tubes in each case run between a first region and a second region in the reactor vessel. For the electrical heating of the tube sections, the tube sections in the first region can be electrically connected to (a) current connection(s) of a current source. In the first region, current feed arrangements are provided; in each case one or in each case one group of the tube sections are electrically connected, and each comprise (a) contact passage(s) that in each case adjoin(s) at least one of the tube sections in the first region. A wall of the contact passages in each case is connected to a current feed element that has a rod-shaped section that runs at a wall passage through a wall of the reactor vessel.

Reactor and method for carrying out a chemical reaction

A reactor has a reactor vessel and one or more reaction tubes. One or more power input elements are guided into the reactor vessel for the electrical heating of the reaction tube(s). The one or more power input elements each have a rod-shaped section, and the rod-shaped section(s) each run in a respective wall passage through a wall of the reactor vessel. A connection chamber into which the rod-shaped section(s) project is arranged outside the reactor vessel and adjacent to the wall of the reactor vessel through which the rod-shaped section(s) run in their wall passages. Gas feed means apply an inerting gas to the connection chamber, and the wall passages with the rod-shaped sections received therein in a longitudinally-movable manner are designed to be gas-permeable so that at least a portion of the inerting gas fed into the connection chamber flows out into the reactor vessel.

A reactor for carrying out a chemical reaction has a reactor vessel, one or more reaction tubes and means for the electrical heating of the one or more reaction tubes. The reactor vessel has one or more discharge orifices which are permanently open or are set up to open above a preset pressure level, and gas feed means are provided, which are set up to feed an inerting gas into an interior of the reactor vessel.

The invention relates to a process for treating a waste lye of a lye scrub using an oxidation reactor (), the waste lye and oxygen or an oxygen-containing gas mixture being introduced into the oxidation reactor () and steam being introduced into the oxidation reactor (). It is provided that the steam is at least partially introduced by means of a steam feeding device (), which has a cylindrical section () with a centre axis () and a wall (), the centre axis () being aligned perpendicularly, a number of groups of openings () being formed in the wall, each of the groups comprising a number of the openings (), and the number of openings () of each of the groups being arranged in one or more planes () that is or are in each case aligned perpendicularly to the centre axis (). A corresponding installation and also a corresponding oxidation reactor () are likewise the subject of the present invention.

Process and device for treating a waste lye

In a process as disclosed according to the present invention, gases or gas mixtures used to form a reactant mixture in an at least temporarily ignitable composition are fed into a mixing chamber () through the passages () in a boundary wall () of the mixing chamber () and by means of one or more feed conduits () which have feed orifices () and extend into the mixing chamber (), respectively. The present invention likewise provides a corresponding reactor ().

Method and system for forming and for catalytically reacting a reactant mixture&#x2014;embodiment of the reactor

A process for producing one or more olefins is proposed in which a reaction input containing one or more paraffins is formed and in which a portion of the paraffin(s) present in the reaction input is converted by oxidative dehydrogenation into the olefin(s) to obtain a process gas, wherein the process gas contains at least the olefin(s), the unconverted paraffin(s), oxygen and carbon monoxide and wherein at least a portion of the process gas is subjected to a low temperature separation in which at an operating pressure level one or more gas fractions enriched in oxygen and carbon monoxide compared to the process gas are formed. It is provided that in the low temperature separation in the formation and/or for the conduction of the or at least one of the gas fractions one or more containers and/or one or more conduits having a burst pressure of at least ten times the operating pressure level are used and that the container or at least one of the containers via the or at least one of the conduits is connected to one or more heat exchangers, wherein a total length of the or of the at least one conduit between the or the at least one container and the heat exchanger(s) is not more than fifty times the internal diameter of said conduit. A corresponding plant () likewise forms part of the subject matter of the invention.

Method and system for producing olefins

The invention relates to a method for producing butadiene from n-butenes having the steps:

Method for preparing 1,3-butadiene from N-butenes by oxidative dehydrogeneation

The invention relates to a process for producing butadiene from n-butenes which comprises the steps of:

Process for preparing 1,3-butadiene from n-butenes by oxidative dehydrogenation

Method for preparing 1,3-butadiene from n-butenes by oxidative dehydrogenation

A process for preparing butadiene from n-butenes, comprising the steps of:

The present invention relates to a method for oligomerization of ethylene, comprising the steps:

Method for oligomerization of ethylene

The invention relates to a process for preparing linear &#x3b1;-olefins, wherein ethyleneis conducted into the oligomerization reactorin the liquid phase. The oligomerization reactorhas a mechanical stirrerin order to ensure optimal mixing of the liquid ethylene and of the catalyst in the liquid phase. From the top of the oligomerization reactor, vaporized ethylene is drawn off together with light &#x3b1;-olefins and a small proportion of the organic solvent. The gas mixture drawn off from the top of the reactoris condensed together with gaseous fresh ethyleneby means of heat exchangerand separator. The liquid phase drawn off from the separatoris conducted by means of circulation pumpas liquid ethylene inputback into the oligomerization reactor. The liquid products of the oligomerization reaction are drawn offlaterally from the base of the reactor

Process for preparing linear &#x3b1;-olefins

Valve arrangement for a system which is loaded with fluid, for connecting a first pressure region to a second pressure region by means of a first valve and a second valve connected in series. A third valve connects a region between the first valve and the second valves to a third pressure region. The first valve closes when a pressure which prevails on the side of the second pressure region is at least as high as a pressure which prevails on the side of the first pressure region. The first valve is coupled to the second valve so that the second valve closes when the first valve closes. The second valve is coupled to the third valve so that the third valve opens when the second valve closes.

Valve arrangement

The present invention relates to a method for preparing linear alpha-olefins (LAO) by oligomerization of ethylene in the presence of solvent and homogenous catalyst, comprising the steps of: (i) feeding ethylene, solvent and catalyst into an oligomerization reactor, (ii) oligomerizing the ethylene in the reactor, (iii) removing a reactor outlet stream comprising solvent, linear alpha-olefins, ethylene, and catalyst from the reactor via a reactor outlet piping system, (iv) transferring the reactor outlet stream to a catalyst deactivation and removal step, and (v) deactivating and removing the catalyst from the reactor outlet stream, characterized in that at least one organic amine is added into the oligomerization reactor and/or into the reactor outlet piping system.

Method for preparing linear alpha-olefins

A catalyst composition and a process for di-, tri- and/or tetramerization of ethylene, wherein the catalyst composition comprises a chromium compound, a ligand of the general structure RRP&#x2014;N(R)&#x2014;P(R)&#x2014;N(R)&#x2014;PRR, or any cyclic derivatives thereof, wherein at least one of the P or N atoms of the PNPNP-unit is member of a ring system, the ring system being formed from one or more constituent compounds of the ligand by substitution, and a co-catalyst or activator.

Catalyst composition and process for di-, tri- and/or tetramerization of ethylene

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Hohenschäftlarn, Germany

Anton Wellenhofer