The present invention discloses an equipment and process for preparing silicon oxides, and relates to the field of chemical equipments. Said equipment comprises at least one tank having opening(s) at at least one end thereof and comprising a reaction unit and a collection unit, wherein the reaction unit is used for placing raw materials therein; and the collection unit is used for placing a collector therein which is placed at the opening end of the tank; and the reaction unit is placed away from the opening end of the tank and placed inside a heating furnace; the collection unit and opening(s) are both placed outside the heating furnace; the tank is vacuumized via a port; and a tank lid is used for opening or closing the opening(s) of the tank. The preparation process uses such equipment. The present invention solves the problems of great energy consumption and low efficiency caused by the fact that the previous equipment and process for preparing silicon oxides are unable to achieve continuous production.

The present invention discloses an equipment and process for preparing silicon oxides, and relates to the field of chemical equipments. Said equipment comprises at least one tank having opening(s) at at least one end thereof and comprising a reaction unit and a collection unit, wherein the reaction unit is used for placing raw materials therein; and the collection unit is used for placing a collector therein which is placed at the opening end of the tank; and the reaction unit is placed away from the opening end of the tank and placed inside a heating furnace; the collection unit and opening(s) are both placed outside the heating furnace; the tank is vacuumized via a port; and a tank lid is used for opening or closing the opening(s) of the tank. The preparation process uses such equipment. The present invention solves the problems of great energy consumption and low efficiency caused by the fact that the previous equipment and process for preparing silicon oxides are unable to achieve continuous production.

Provided is a fuel tank producing apparatus capable of uniformly heating a tank container in a short period of time. The fuel tank producing apparatus includes a heat curing furnace for heating the tank container and a hot air generator for generating hot air. The heat curing furnace is internally provided with a nozzle for blowing the hot air onto the surface of the tank container, and externally provided with a rotating portion for rotating the tank container about the central axis thereof. The nozzle is located at a position displaced to the left relative to the vertical direction to the central axis of the tank container as viewed from the direction of the central axis of the tank container. The rotating portion is configured to rotate the tank container in the reverse direction of a direction in which the hot air is blown from the nozzle.

The present invention discloses an equipment and process for preparing silicon oxides, and relates to the field of chemical equipments. Said equipment comprises at least one tank having opening(s) at at least one end thereof and comprising a reaction unit and a collection unit, wherein the reaction unit is used for placing raw materials therein; and the collection unit is used for placing a collector therein which is placed at the opening end of the tank; and the reaction unit is placed away from the opening end of the tank and placed inside a heating furnace; the collection unit and opening(s) are both placed outside the heating furnace; the tank is vacuumized via a port; and a tank lid is used for opening or closing the opening(s) of the tank. The preparation process uses such equipment. The present invention solves the problems of great energy consumption and low efficiency caused by the fact that the previous equipment and process for preparing silicon oxides are unable to achieve continuous production.

The present invention discloses an equipment and process for preparing silicon oxides, and relates to the field of chemical equipments. Said equipment comprises at least one tank having opening(s) at at least one end thereof and comprising a reaction unit and a collection unit, wherein the reaction unit is used for placing raw materials therein; and the collection unit is used for placing a collector therein which is placed at the opening end of the tank; and the reaction unit is placed away from the opening end of the tank and placed inside a heating furnace; the collection unit and opening(s) are both placed outside the heating furnace; the tank is vacuumized via a port; and a tank lid is used for opening or closing the opening(s) of the tank. The preparation process uses such equipment. The present invention solves the problems of great energy consumption and low efficiency caused by the fact that the previous equipment and process for preparing silicon oxides are unable to achieve continuous production.

Coke oven corbel structures include an assembly of multiple stacked tiers of refractory blocks defining a plurality of substantially vertically oriented central flues and a plurality of diagonally oriented lateral flues. At least one tier of refractory blocks in the assembly includes a plurality of tongue-and-groove interconnected refractory blocks. This plurality of interconnected refractory blocks of the at least one tier comprise mutually substantially orthogonal faces defining an edge and respectively including an elongate tongue protruding outwardly therefrom and an elongate groove recessed therein. The elongate tongue and groove include respective adjacent ends which co-terminate with one another at the edge defined by the mutually orthogonal faces of the refractory blocks.

Coke oven corbel structures include an assembly of multiple stacked tiers of refractory blocks defining a plurality of substantially vertically oriented central flues and a plurality of diagonally oriented lateral flues. At least one tier of refractory blocks in the assembly includes a plurality of tongue-and-groove interconnected refractory blocks. This plurality of interconnected refractory blocks of the at least one tier comprise mutually substantially orthogonal faces defining an edge and respectively including an elongate tongue protruding outwardly therefrom and an elongate groove recessed therein. The elongate tongue and groove include respective adjacent ends which co-terminate with one another at the edge defined by the mutually orthogonal faces of the refractory blocks.

Contemplated devices and methods reduce heat loss and energy demand of a carbon baking ring furnace by employing a preferably internal bypass conduit that feeds a portion of a heated cooling air stream from the cooling zone directly to the flue ducts of the firing and/or pre-heat zones.

Contemplated devices and methods reduce heat loss and energy demand of a carbon baking ring furnace by employing a preferably internal bypass conduit that feeds a portion of a heated cooling air stream from the cooling zone directly to the flue ducts of the firing and/or pre-heat zones.

An industrial furnace (1) into which protective gas is admitted for the heat treatment of batches (5) of metal workpieces is described. The heat treating furnace includes an entrance lock (2) which can be sealed with respect to the surrounding environment by means of a first gas-tight closure device (2.2.1). The heat treating furnace also includes a third gas-tight closure device (3.1) disposed between a heat treatment chamber (3) of the furnace and a quenching facility (4) at the exit of the heat treatment chamber. With the foregoing arrangement a pressure of the protective gas admitted into the heat treatment chamber (3) can be maintained during loading and unloading of a batch of metal workpieces (5). The entrance lock may be configured as a dual-chamber vertical arrangement or as a single chamber horizontal arrangement.