The invention relates to a dirt precipitator (100) for a highly viscous medium, having a housing comprising a front housing element (30; 30) that comprises at least one inlet channel (33) and a rear housing element (20) that comprises at least one outlet channel (23), and having a screen wheel (10; 10) rotatably mounted between the housing elements (20, 30; 30) having a number n of screen positions disposed in a ring zone, on each of which at least one screen opening (11.1, . . . , 11.12) having at least one screen insert element is provided. The inlet channel (33), the outlet channel (23), and the screen opening (11.1, . . . , 11.12) are disposed flush one after the other in at least one working position and form a flow channel. In all positions of the screen wheel (10; 10), more than 50% of the screen openings (11.1, . . . , 11.12) are always able to be permeated, and are impinged by flow from at least one inlet channel and from which at least one outlet channel leads.

An improved process for the preparation of high viscosity (i.e., greater than 1 million mPa.Math.s at 25 C.) silanol-terminated silicone polymers and copolymers, often referred to in the industry as silanol-terminated silicone polymer gums. The silanol-terminated silicone polymer gums are made by the ring-opening polymerisation of organocyclosiloxane oligomers (alternatively referred to as cyclic siloxane oligomers) using a conical screw dump extruder (1). It also relates to silanol-terminated silicone polymer gums made by the process.

A stream of seed may be maintained at a metered flow rate through multiple stages of a treatment process. These multiple stages include dispensing, first application of fluid, second application of fluid, and seed transport. Seed transport may be accomplished through a conveyor configured to maintain the metered flow rate while providing static mixing, drying, and conditioning of the treated seed. The metered stream of seed may be treated within a first treatment applicator where a first wet treatment is applied, transferred through the incline conveyor, and treated again within a second treatment applicator where a second wet treatment is applied. Overtreating in multiple stages may layer consecutive seed treatments around the treated seed. A predetermined amount of seed treatment may be applied to the coated seed based on the metered flow rate established. Maintaining the metered flow rate through multiple stages eliminates the need for multiple metering steps.

An agricultural incline conveyor having belt guards extending longitudinally through a curvilinear portion from a tail inlet to a head outlet. The belt guards protect linear edges of a belt within the curvilinear portion during mixing operations. A plurality of mixing baffles positioned within the curvilinear portion induce turbulent backflow of a metered stream of seed being transported through the curvilinear portion. The longitudinal guards prevent the loss of transported seed from entering between the belt and a trough of the curvilinear portion.

Waste mixing processing equipment has a waste mixing device and a feeding device. The waste mixing device has a major mixing set, a sub-mixing set, and an extruding-and-shaping set arranged in sequence. The major mixing device and the sub-mixing device each have a y-shaped mixing passage in a base and tapering toward a discharging port, a driving screw, and a driven screw obliquely disposed therein. Waste and additives/fillers are fed into the major mixing set by proportion, and are mixed sequentially through the major mixing set and the sub-mixing set. The waste and the additives/fillers are mixed, extruded, and conveyed by the driving screw and the driven screw in the y-shaped mixing passages of the major/sub-mixing sets, whereby mixing efficiency is improved.

The invention relates to a process for producing an extruded sulfur-crosslinkable rubber mixture, comprising the following process steps: A) producing a sulfur-crosslinkable rubber mixture by means of a mixer or providing a sulfur-crosslinkable rubber mixture, where the temperature of the sulfur-crosslinkable rubber mixture is less than 35 C., B) contactlessly adjusting the temperature of the sulfur-crosslinkable rubber mixture produced or provided in step A) to at least 40 C. in a temperature adjustment unit, C) measuring the temperature of the rubber mixture in the temperature adjustment unit and D) feeding the sulfur-crosslinkable rubber mixture that has been measured in step C) into an extrusion unit at a temperature of 35 C. or more and extruding the fed rubber mixture in the extrusion unit. The invention further relates to an apparatus for performing the process and to the use of the apparatus.

The invention relates to a process for producing an extruded sulfur-crosslinkable rubber mixture, comprising the following process steps: A) producing a sulfur-crosslinkable rubber mixture by means of a mixer or providing a sulfur-crosslinkable rubber mixture, where the temperature of the sulfur-crosslinkable rubber mixture is less than 35 C., B) contactlessly adjusting the temperature of the sulfur-crosslinkable rubber mixture produced or provided in step A) to at least 40 C. in a temperature adjustment unit, C) measuring the temperature of the rubber mixture in the temperature adjustment unit and D) feeding the sulfur-crosslinkable rubber mixture that has been measured in step C) into an extrusion unit at a temperature of 35 C. or more and extruding the fed rubber mixture in the extrusion unit. The invention further relates to an apparatus for performing the process and to the use of the apparatus.

A mixing and cooling system (1) includes a mixing and screw-extrusion machine (10) with a mixer (12) having a converging conical twin screw; a ram (30) that moves along the inside of an introduction hopper (24) of the machine; a roller nose system disposed just downstream of an outlet (25) of the mixer to form a sheet (112) of the mixture exiting the mixer; and a mobile sleeve or sleeves (34) that move in a linear movement relative to the outlet. The system also includes a cooling system with a spray installation(s) (102, 104) that delivers water at a predetermined rate to the sheet exiting the machine; a suction installation(s) proportionate to each spray installation; and at least one transport means (114, 116) that transports the sheet in a predetermined direction.

The invention relates to a device for producing and processing a multi-component mixture, the device comprising a mixing chamber which has an outlet, wherein the device has a closure element which can be moved in the direction of a longitudinal axis L of the mixing chamber in order to open or close the outlet of the mixing chamber; wherein the device has an apparatus for controlling an axial speed of the closure element, the apparatus comprising: a hydraulic system in which a hydraulic fluid is guided; a cylinder which is connected to the nozzle closure element and cooperates with at least one chamber of the hydraulic system; and a controllable throttle gap arranged in the hydraulic system.

A screw extruder includes a tapered screw having a shaft portion and a wing portion, a driving device that rotates the tapered screw, a casing having a passage port through which a material passes, and a die plate attached to the casing so as to close the passage port. The die plate has a first discharge perforation arranged at a position corresponding to the tapered screw. During rotation of the tapered screw, size of an overlapping region between a top surface of the wing portion of the tapered screw and the first discharge perforation when viewed in a material extrusion direction changes periodically. A material extruded by the tapered screw is cut by increase in the overlapping region between the first discharge perforation and the top surface of the wing portion.