Patent classifications
B01J8/42
Process for producing humic acid salts with fluidizing solid phase reaction
The present invention utilizes a high-speed intensive mixer in a fluidizing-type, solid-phase, neutralization reactor to blend solid-state alkali hydroxide with any humic acid sources. The final product is a dry humic acid salt. The purpose of this innovative method is to eliminate a series of complicated unit operations commonly employed by the traditional process. These removed steps may include dissolving caustic soda, mixing in a paste-like formation, extrusion, granulation, drying, and grinding, etc. The invention contributes to a simplified flowsheet, resulting in sharply reduced equipment investment, plant space, and labor and energy costs. All of these factors coupled with increased productivity will drastically lower the overall production cost. Also, the reduction of dust pollution will greatly minimize the impact in environmental protection and safety issues.
Process for producing humic acid salts with fluidizing solid phase reaction
The present invention utilizes a high-speed intensive mixer in a fluidizing-type, solid-phase, neutralization reactor to blend solid-state alkali hydroxide with any humic acid sources. The final product is a dry humic acid salt. The purpose of this innovative method is to eliminate a series of complicated unit operations commonly employed by the traditional process. These removed steps may include dissolving caustic soda, mixing in a paste-like formation, extrusion, granulation, drying, and grinding, etc. The invention contributes to a simplified flowsheet, resulting in sharply reduced equipment investment, plant space, and labor and energy costs. All of these factors coupled with increased productivity will drastically lower the overall production cost. Also, the reduction of dust pollution will greatly minimize the impact in environmental protection and safety issues.
PHOTOCATALYTIC REACTOR STATOR AND METHOD OF USE
An improved photocatalytic reactor stator having a first surface and an opposing second surface, and at least one channel extending between the first surface and the second surface to allow fluid flow through the stator. The at least one channel may be configured to redirect the fluid flow in a direction substantially parallel to the first and/or second surface. This improved photocatalytic reactor stator improves the performance of a photocatalytic reactor by increasing the mobility of the photocatalyst and thereby increasing the surface area of the catalyst that is exposed to the reactant and the UV light source.
PHOTOCATALYTIC REACTOR STATOR AND METHOD OF USE
An improved photocatalytic reactor stator having a first surface and an opposing second surface, and at least one channel extending between the first surface and the second surface to allow fluid flow through the stator. The at least one channel may be configured to redirect the fluid flow in a direction substantially parallel to the first and/or second surface. This improved photocatalytic reactor stator improves the performance of a photocatalytic reactor by increasing the mobility of the photocatalyst and thereby increasing the surface area of the catalyst that is exposed to the reactant and the UV light source.
Fluidized bed reactor and a process using same to produce high purity granular polysilicon
The present invention relates to a fluidized bed reactor, comprising a reaction tube, a distributor and a heating device, the reaction tube and the distributor at the bottom of the reaction tube composing a closed space, the distributor comprising a gas inlet and a product outlet, and the reaction tube comprising a tail gas outlet and a seed inlet at the top or upper part respectively, characterized in that the reaction tube comprises a reaction inner tube and a reaction outer tube, and the heating device is an induction heating device placed within a hollow cavity formed between the external wall of the reaction inner tube and the internal wall of the reaction outer tube, wherein the hollow cavity is filled with hydrogen, nitrogen or inert gas for protection, and is able to maintain a pressure of about 0.01 to about 5 MPa; and also to a process of producing high purity granular polysilicon using the reactor. The fluidized bed reactor according to the present invention uses induction heating to heat directly the silicon particles inside the reaction chamber, such that the temperature of the reaction tube is lower than that inside the reaction chamber, which accordingly avoids deposition on the tube wall and results in more uniform heating, and thus is useful for large diameter fluidized bed reactors with much increased output for a single reactor.
Fluidized bed reactor and a process using same to produce high purity granular polysilicon
The present invention relates to a fluidized bed reactor, comprising a reaction tube, a distributor and a heating device, the reaction tube and the distributor at the bottom of the reaction tube composing a closed space, the distributor comprising a gas inlet and a product outlet, and the reaction tube comprising a tail gas outlet and a seed inlet at the top or upper part respectively, characterized in that the reaction tube comprises a reaction inner tube and a reaction outer tube, and the heating device is an induction heating device placed within a hollow cavity formed between the external wall of the reaction inner tube and the internal wall of the reaction outer tube, wherein the hollow cavity is filled with hydrogen, nitrogen or inert gas for protection, and is able to maintain a pressure of about 0.01 to about 5 MPa; and also to a process of producing high purity granular polysilicon using the reactor. The fluidized bed reactor according to the present invention uses induction heating to heat directly the silicon particles inside the reaction chamber, such that the temperature of the reaction tube is lower than that inside the reaction chamber, which accordingly avoids deposition on the tube wall and results in more uniform heating, and thus is useful for large diameter fluidized bed reactors with much increased output for a single reactor.
DIRECTLY ELECTRICAL HEATED REACTOR
The invention relates to a reactor comprising a moving bed of solid particles that move in the direction of gravitation, and to a method for heating a reactor that comprises a moving bed, for the purpose of pyrolysis reactions.
DIRECTLY ELECTRICAL HEATED REACTOR
The invention relates to a reactor comprising a moving bed of solid particles that move in the direction of gravitation, and to a method for heating a reactor that comprises a moving bed, for the purpose of pyrolysis reactions.
Flow-promoting device, a reactor arrangement and the use of such flow-promoting device
The invention refers to a flow-promoting device (100; 100; 100″) for performing a biological or chemical transformation, or physical or chemical trapping from, or release of agents to, a fluidic medium. The flow-promoting device (100; 100; 100″) comprises a ferromagnetic material (5) and a retaining structure (1; 1; 1″), the retaining structure having a compartment (9; 9″) defined by a permeable material (11; 11″). The retaining structure (1; 1; 1″) comprises a top wall (3; 3″) and a circumferential side wall (4; 4″), wherein the top wall (3; 3″) and the circumferential side wall (4; 4″) is formed mainly by said permeable material (11; 11″). The compartment (9; 9″) of the retaining structure (1; 1; 1″) is arranged to contain at least one fluid-permeable solid reaction member.
Flow-promoting device, a reactor arrangement and the use of such flow-promoting device
The invention refers to a flow-promoting device (100; 100; 100″) for performing a biological or chemical transformation, or physical or chemical trapping from, or release of agents to, a fluidic medium. The flow-promoting device (100; 100; 100″) comprises a ferromagnetic material (5) and a retaining structure (1; 1; 1″), the retaining structure having a compartment (9; 9″) defined by a permeable material (11; 11″). The retaining structure (1; 1; 1″) comprises a top wall (3; 3″) and a circumferential side wall (4; 4″), wherein the top wall (3; 3″) and the circumferential side wall (4; 4″) is formed mainly by said permeable material (11; 11″). The compartment (9; 9″) of the retaining structure (1; 1; 1″) is arranged to contain at least one fluid-permeable solid reaction member.