Continuous-flow reactor for high viscosity materials

A reactor for continuous processing of high viscosity materials comprising:

• an elongated hollow vessel having a longitudinal axis, longitudinal side wall means, transverse end wall means, an inlet at one end, an outlet at the opposite end for the introduction and discharge of the process material under pressure, and a rotary drive shaft extending through said vessel along said longitudinal axis;
• a plurality of flat imperforate transverse barrier plates within said vessel and forming, in conjunction with the vessel wall means, at least two reaction stages, the first stage disposed adjacent said inlet and a second stage adjacent the outlet, one of said barrier plates having clearance between its outer periphery and the longitudinal vessel side wall to constitute an end orifice providing a restricted passage for uniform egression of a first portion of the material from the first stage in a direction away from said inlet and into said second stage at a predetermined fixed rate, another of said barrier plates having clearance between its outer periphery and the longitudinal vessel side wall to constitute an end orifice providing a restricted passage adjacent to said outlet for the uniform egression of a predetermined portion of the process material from the second stage in a direction away from said inlet and towards said outlet;
• mixing means mounted within each reaction stage on said elongated drive shaft, said shaft driving said mixing means at a given speed for homogeneously agitating and recirculating a second portion of the process material which remains in each stage after egression of said first portion from said stage, said mixing means comprising:
• a longitudinal draft tube mounted concentrically on said shaft, said draft tube being spaced from the wall means forming said stage and defining a continuous recirculating flow path for process material within the stage, said path including an advancing annular passage between said tube and the longitudinal side wall means of the vessel and a return annular passage within said tube;
• a helical screw having a pitch in one direction with its axis longitudinal mounted concentrically on said drive shaft and extending between the drive shaft and the draft tube;
• and
• helical agitator means having a pitch opposite to that of the helical screw mounted with its axis longitudinal and mounted concentrically on said drive shaft in the space between the draft tube and vessel longitudinal side wall means,
• whereby in each stage upon driving said drive shaft, said agitator advances the first and second portions of the process material in said advancing passage of said path exteriorly of the tube and said helical screw returns said second portion of the process material in said return passage of said path interiorly of the tube,
• the width of said shaft tube, the pitch of said helical screw, the speed of said drive shaft, the size of the orifice and the viscosity and pressure of the material introduced through said inlet cooperating to control the flow in said path and determine the ratio between said first and second portions of said material and thereby the residence time of the material in each stage of said reactor.