Siemens Aktiengesellschaft

Siemens Energy Global Gmbh & Co. Kg

Siemens Mobility Gmbh

Alexander Tremel

Peter Wasserscheid

Thomas Hammer

Manfred Baldauf

Jakob Albert

Uwe Lenk

Katharina Stark

Marc Hanebuth

Nicolas Vortmeyer

Erik Wolf

Jenny Reichert

Jochen Schaefer

Florian Reissner

Katharina Meltzer

Markus Ziegmann

Lukas Glöser

Jochen SCHÄFER

Various embodiments may include a reactor comprising: a reaction chamber having a lower region defining a sorbent collection zone; a first feed device supplying reactants to the reaction chamber; a second feed device supplying a liquid sorbent to the reaction chamber; a discharge device connected to the sorbent collection zone for removing sorbent from the sorbent collection zone; and a cooling device for cooling the sorbent in the reaction chamber.

Reactor with cooling device

The present disclosure relates to converting equilibrium-limited reactions. Various embodiments may include methods and apparatus for such reactions, such as a method for converting equilibrium-limited reactions comprising: delivering a catalyst material to a reaction zone of a reactor; delivering starting materials into the reaction zone; reacting the materials to form a product; introducing a sorbent into the reactor; taking up the products with the sorbent; and collecting the sorbent once it is loaded with products in a collection zone of the reactor. In some embodiment, the reaction zone is separated from the collection zone in the reactor.

Converting equilibrium-limited reactions

The present disclosure relates to chemical synthesis. The teachings thereof may be embodied in methods for chemical synthesis and/or reactors for synthesis. The teaching may increase the conversion of equilibrium-limited reactions in a single pass through a synthesis reactor. For example, a method may include: introducing a synthesis reactant into a reaction chamber with a prevailing pressure p1; forming a synthesis product; discharging the product and any unreacted reactant; separating the product from the unreacted reactant; and introducing the unreacted reactant into a second reaction chamber with a prevailing pressure p2 lower than the pressure p1.

Chemical synthesis and synthesis reactors

Various embodiments may include a reactor for carrying out equilibrium-limited reactions comprising: a reaction chamber for receiving a catalyst; a sorption chamber for receiving a sorption agent; a feedstock feeding device; a sorption agent feeding device; and a gas-permeable element separating the reaction chamber from the sorption chamber, wherein the gas-permeable element repels particles of the sorption agent.

Reactor for carrying out equilibrium-limited reactions

Various embodiments include a reactor for implementation of equilibrium-limited reactions comprising: a reaction space; a reactant feed; an outlet for reaction products; a device for accommodating catalyst material; and a stirrer device comprising: a hollow shaft with a gas inlet opening at one end of the hollow shaft; a first stirrer paddle with gas exit orifices mounted on the hollow shaft; and a second stirrer paddle mounted on the hollow shaft proximate the device for accommodating the catalyst material.

Reactor and method for equilibrium-limited reactions

The present disclosure relates to chemical synthesis. Various embodiments of the teachings thereof may include the synthesis of methanol, generated from hydrogen and a carbonaceous gas. For example, a method may include: compressing gaseous starting materials to an operating pressure of at least 200 bar; supplying the starting materials to a synthesis reactor; removing a product mixture from the synthesis reactor in a liquid state; withdrawing mechanical energy from the product mixture by reducing a pressure of the product mixture; and using the mechanical energy to compress the gaseous starting materials.

Process and system for chemical synthesis

A device for the separation of water, in particular water vapor, from a fluid flow containing water, in particular water vapor, may include at least a water-permeable membrane body that delimits at least one membrane body interior space, wherein at least one hydrophobic fluid is located in the membrane body interior space for receiving water, in particular water vapor, which exits the fluid flow and passes through the membrane body into the membrane body interior space.

Device for the separation of water from a fluid flow containing water

A method and a device for discharging a thermal stratification storage tank are provided, wherein a first thermal stratification storage tank has a first temperature in a first subsection and a second temperature in a second subsection, when the working fluid of an organic Rankine cycle in the liquid aggregate state in a fluid heat transfer medium of the first thermal stratification storage tank is introduced into the first or second subsection and brought into direct material contact with the heat transfer medium, wherein at the second temperature in the second subsection the pressure in the first thermal stratification storage tank is less than or equal to the vapor pressure of the working fluid.

Method and device for discharging a stratified thermal storage tank

A method for operating a steam turbine plant including a steam turbine and a steam generator allows a power reserve to be provided whilst simultaneously maintaining a high level of efficiency in the normal mode of operation. The steam turbine plant includes a heat reservoir which is associated with the steam turbine, from which the steam is removed and is fed to the steam turbine. The steam is fed to the steam turbine when the steam generator is not in operation.

Method for operating a steam turbine plant

A control system for controlling the temperature in a high-temperature battery to which hot air is supplied via an air duct system or in a high-temperature electrolyzer to which hot air is supplied via an air duct system is provided. The control system includes at least two temperature probes designed to detect the temperature at two different points in the air duct system, at least one first air-conditioning unit for physically conditioning the air, mounted in the air duct system upstream of the high-temperature battery or high-temperature electrolyzer, and a recirculation duct which recirculates hot air discharged from the high-temperature battery or high-temperature electrolyzer to a point in the air duct system upstream of the high-temperature battery or high-temperature electrolyzer and feeds the hot air back into the air duct system. The control system controls the first air-conditioning unit in accordance with the temperatures detected by the temperature probes.

Temperature control system for a high-temperature battery or a high-temperature electrolyzer

A power station arrangement is provided having an energy generation unit for generating useful thermal energy on the basis of physical and/or chemical processes, a high-temperature storage unit to be at least partially supplied with heat for regular operation, particularly a metal oxide/air storage unit, and a piping system for thermally coupling the energy generation unit to the high temperature storage unit.

Power station arrangement with high-temperature storage unit

At least one heat pipe for removing heat is led into a reactor housing of a fluidized bed reactor, so that the temperature in the reactor housing can be controlled.

Growing community of inventors

Möhrendorf, Germany

Alexander Tremel