Outotec Oyj

Anellotech, Inc.

Outotec (finland) Oy

Metso Outotec Finland Oy

Michael Missalla

Guenter Schneider

Andreas Orth

Nikola Anastasijevic

Edgar Gasafi

Pekka Hiltunen

Roger Bligh

Cornelis Klett

Michael Stroeder

Peter Sturm

Jean-Paul Nepper

Erwin Schmidbauer

Leslaw Mleczko

Linus Perander

Jean Claude Hein

Bernd Reeb

Robert Maduta

Ludwig Hermann

Günter Schneider

Lilli Sacharow

Karl-Ernst Wirth

Omar M Basha

Isabella Vandermaelen

Jan Jarzembowski

Mithat Schmitz

Rene-Arndt Erler

Rolf Gilgen

Michael STRÖDER

Torsten Liebmann

Michael Stroder

A process that separates the fillers found in plastics from catalyst and the gases in a fluid bed catalytic pyrolysis process for the conversion of waste plastics, polymers, and other waste materials to useful chemical and fuel products such as paraffins, olefins, and aromatics such as BTX, is described.

High efficiency process for separating fillers from catalyst and gases in a fluid bed catalytic pyrolysis process

A plant for refining raw materials containing organic constituents includes a reactor configured to receive raw materials; a furnace configured to receive solids and fuel from the reactor; a return conduit configured to recirculate hot solids generated in the furnace to the reactor; and a sealing device configured to separate an oxidizing atmosphere of the furnace from an atmosphere of the reactor. The sealing device includes: a downpipe disposed between the furnace and the reactor, the downpipe being configured to withdraw a stream of solids from the furnace; a rising pipe disposed near a bottom of the downpipe and branching off there from to a top, the rising pipe being configured to transport a fluidized stream of solids to the reactor; and a conveying gas supply disposed below the rising pipe, the conveying gas supply being configured to fluidize a stream of solids withdrawn from the furnace.

Process and plant for refining raw materials containing organic constituents

A plant for chemical or physical treatment of granular solids includes a fluidized-bed reactor, a solids supply conduit and a central gas supply tube. A cooling tube is disposed relative to the gas supply tube so as to form an annular cooling duct, which is configured to cool the gas supply tube and the process gas and is connected with a coolant source configured to supply a coolant with a temperature of below about 400&#xb0; C. Outlet openings are disposed in the cooling tube. The fluidized-bed reactor is a Venturi reactor in which the cooling tube opens into a flared portion with the outlet openings connecting the annular cooling duct with the reactor interior. The cooling tube adjoins the gas supply tube and extends substantially parallel to the flared portion of the reactor.

Process and plant for the thermal treatment of fine-grained solids

A process for refining raw materials containing at least one of oil and bitumen includes supplying the raw materials to a reactor and volatilizing fuel gas in the reactor at a temperature of from 300 to 1000&#xb0; C. and a pressure of from 0.001 to 1 bar. Solids remaining in the reactor, including non-evaporated fractions of heavy hydrocarbons, are introduced into a furnace. A staged combustion of the non-evaporated fractions of heavy hydrocarbons is performed in a substoichiometric stage and in a superstoichiometric stage in the furnace at a furnace temperature of from 600 to 1500&#xb0; C. as to obtain hot solids in the furnace. The hot solids are recirculated from the furnace into the reactor. A sealing device separates an oxidizing atmosphere of the furnace from an atmosphere of the reactor.

Process and plant or refining raw materials containing organic constituents

A method for producing a clinker substitute for use in cement production includes predrying clay with an iron content &#x3e;1.5 wt-% in a form of iron oxides and a kaolinite content &#x3c;40 wt-% to a moisture &#x3c;10 wt-%. The clay is comminuted to a grain size &#x3c;2 mm. The clay is calcined by thermal treatment in a furnace at a temperature of 600 to 1000&#xb0; C. The clay is thermally treated under reducing conditions at a temperature of 600 to 1000&#xb0; C. so as to form a reduction product. The reduction product is intermediately cooled to a temperature &#x3c;300&#xb0; C. and finally cooled.

Clinker substitute based on calcined clay

An apparatus for the treatment of at least one of solids and gases includes a fluidized-bed reactor configured to fluidize the solids using fluidizing gas and to at least one of thermally and chemically treat the solids. A centrifugal separator is configured to separate the fluidizing gas and the solids from each other. A transfer duct connects the fluidized-bed reactor and centrifugal separator to each other. The transfer duct has a trapezoidal cross-section in a vertical direction and in a horizontal direction. The transfer duct branches off from the fluidized bed reactor with a cross-section having a horizontal dimension that is greater than a vertical dimension. The cross-section of the transfer duct expands downwards in the vertical direction from the fluidized-bed reactor to the centrifugal separator. The cross-section of the transfer duct tapers in the horizontal direction from the fluidized-bed reactor towards the centrifugal separator.

Apparatus for the treatment of solids and/or gases

A process for at least one of a chemical and a physical treatment of fluidizable substances in a reactor. The process includes introducing a hot gas into an interior of the reactor through a gas supply tube and cooling at least one of the hot gas and the gas supply tube with a coolant. The cooling is performed by contacting the hot gas with the coolant so as to provide a temperature of a wall of the gas supply tube at least 50&#xb0; C. lower than a temperature of the gas at an inlet of the gas supply tube facing away from the interior of the reactor.

A process for refining oil-containing includes introducing the oil-containing solids to a reactor so as to expel an oil-containing vapor from the solids at a temperature of 300 to 1000&#xb0; C. The oil-containing vapor expelled from the reactor is supplied to a cracker so as to crack heavy oil components of the oil-containing vapor. The cracked heavy oil components obtained in the cracker are separated and withdrawn from the cracker. The solids left in the reactor and an unevaporated fraction of heavy hydrocarbons are introduced into a furnace. The unevaporated fraction of heavy hydrocarbons in the furnace are burned at a temperature of 600 to 1500&#xb0; C. The solids from the furnace are recirculated into the reactor. A conveying gas is supplied into a rising pipe, wherein the stream of solids withdrawn from the furnace is fluidized by the conveying gas and transported to the reactor through the rising pipe.

Process and plant for refining oil-containing solids

A cyclone for separating sticky particles from gas streams includes an inlet duct having an end in a direction of a particle outlet. The end has a flow cross-section including a triangular expansion that is formed laterally by a vertical of a cylindrical outer wall of the cyclone and by art outer boundary of the cyclone. An outer angle of inclination between the vertical and the outer boundary, proceeding from the end of the inlet duct, is reduced from 30&#xb0; to 0&#xb0; in a flow direction of gas streams. An immersion tube is disposed eccentrically in a direction of the inlet duct.

Cyclone for separating sticky particles from gas streams

A method for controlling at least one of a level of solids and an inventory of solids in a solids tank includes withdrawing a stream of solids from the solids tank via a downer. The stream of solids withdrawn from the solids tank is fluidized at a bottom of the downer by supplying a conveying gas so as to convey the withdrawn stream of solids upward via a riser branching off from the downer, a size of the conveyed stream of solids being adjusted by the supplying of the conveying gas. At least one of the level and the inventory of the solids in the solids tank is used as an adjustment variable of a control circuit and a volume flow of the conveying gas is used as an actuating variable of the control circuit.

Method and apparatus for controlling a stream of solids

A process for producing metal oxide from a metal salt includes supplying a first part of the metal salt to a hydrate drier so as to indirectly heat the first part of the metal salt in the hydrate drier using a heat transfer medium from a first stage of a multi-stage indirect cooler so as to dry the first part of the metal salt in the hydrate drier and so as to control a waste gas temperature of the process. A second part of the metal salt is guided as a partial stream past the hydrate drier. The metal salt is preheated in a first preheating stage and precalcined in a second preheating stage. The metal salt and a fluidizing gas having a temperature of 150&#xb0; C. or less are supplied to a fluidized bed reactor so as to calcine the metal salt to form a metal oxide product. The metal oxide product is cooled in at least one suspension heat exchanger and then in the multi-stage indirect cooler.

Process and plant for producing metal oxide from metal salts

A process for producing metal oxide from metal salts includes cleaning a metal salt in a filter. After cleaning, the metal salt is dried in a drying apparatus. Steam is formed in the drying apparatus. The metal salt is preheated in at least one preheating stage. The metal salt is calcined to metal oxide in a fluidized-bed reactor. The metal oxide is cooled. The steam formed in the drying apparatus is recirculated into the filter.

A method for dividing a stream of solids includes discharging the stream of solids via a first downer. The stream of solids are fluidized at a bottom of the first downer by supplying a first conveying gas. By the first conveying gas, a part of the stream of solids are conveyed to a top of a first riser branching off from the first downer. A remaining part of the stream of solids are discharged via a second downer adjoining the first downer. The remaining stream of solids are fluidized at a bottom of the second downer by supplying a second conveying gas. By the second conveying gas, a part of the remaining part of the stream of solids are conveyed to a top of a second riser branching off from the second downer.

Growing community of inventors

Oberursel, Germany

Michael Missalla