A method for improving the heating efficiency of steam wherein a polyamine represented by the following general formula (1) is caused to be present in a steam system to be used for heating. R.sup.1—[NH—(CH.sub.2).sub.m].sub.n—NH.sub.2 . . . (1) wherein R.sup.1 represents a saturated or unsaturated hydrocarbon group having 10 to 22 carbon atoms; m is an integer of 1 to 8, and n is an integer of 1 to 7; and when n is 2 or more, a plurality of NH—(CH.sub.2).sub.m may be identical or different.

Method for the preparation of dried polymer pellets in a facility having a dryer with a first chamber and a mechanical agitator, and the facility further having a degassing silo with a second chamber, the method includes the steps of guiding a drying gas flow made from or containing a first gas mixture for drying wet polymer pellets into the first chamber, transferring the dried polymer pellets into the second chamber, guiding a second gas mixture for degassing the dried polymer pellets into the second chamber thereby transforming the second gas mixture into a third gas mixture and guiding a portion of the third gas mixture into the first chamber; and process for manufacturing LDPE pellets.

An apparatus for drying materials is disclosed. The apparatus has a chamber which is heated to a temperature sufficient to vaporize the water in the material into steam. The dryer is configured to utilize the steam produced from the material to condition the material. The dryer has two exhaust stacks positioned at opposing ends of the dryer. The removal of exhaust steam at the two opposing ends of the dryer facilitates the migration of moisture within the chamber along a length of the dryer between the two ends. The exhaust stacks can be controlled and adjusted based on feedback from a plurality of pressure differential transmitters installed within the chamber. Methods for drying materials are also disclosed.

A method for drying materials is disclosed. The method comprises introducing a material into a dryer chamber, creating steam from vaporizing moisture in the material by maintaining the chamber at a temperature, conditioning the material using the steam created from vaporing moisture in the material by conveying the material along a length of the chamber from an inlet end to an outlet end, exhausting steam near the inlet end of the chamber, exhausting steam near a dry-end exit end of the chamber, controlling a migration of moisture between the inlet and outlet ends by adjusting an exhaust flow rate near the inlet end of the chamber and/or an exhaust flow rate near the dry-end exit end of the chamber, and withdrawing the material from the chamber.

Disclosed is a slurry drying plant (1) comprising a slurry extruder (3) including a slurry inlet (2) and conveying means (4) arranged to convey the slurry through the slurry extruder (3) and force the slurry out of a plurality of exit openings (5) of the slurry extruder (3) to form a plurality of slurry strings (7), wherein the slurry strings (7) are forced out into a drying chamber (8) in which the plurality of slurry strings (7) is dried. The slurry drying plant (1) further comprises slurry heating means (6) comprising flow means for passing superheated steam past the slurry strings (7) in the drying chamber (8), and inlet pressure detection means (9) for detecting a slurry inlet pressure at the slurry inlet (2). The slurry drying plant (1) also comprises control means (17) arranged to control the conveying speed of the conveying means (4) in response to the slurry inlet pressure. Furthermore, a method for drying slurry and use of a slurry drying plant (1) is disclosed.

A method for cell disruption and extraction of a plant, includes placing plant material on a porous container, placing the porous container into a reaction device, and producing water ion steam of an atmospheric pressure by a water ion generator. The water ion steam infiltrates the porous container and permeates the plant material. The water ion steam penetrate cells of the plant material and breaks the cell wall of the cells, to cause a cell disruption. The residual water ion steam is drained outward from the exhaust pipe of the box.

A dryer for drying dry materials having heating and cooling chambers, wherein the two chambers are sealed gas-tight to each other and/or to the outside environment, a connecting line that fluidically connects the chambers to each other and has a closing valve, a vacuum pump that is actively connected to the cooling chamber, a heat pump that is actively connected to the two chambers, and a steam generator which feeds generated steam via a steam line into the heating chamber,
The steam mixes with moisture of the dry materials in the heating chamber and the resulting moist steam is supplied to the cooling chamber via the connecting line, wherein positive pressure is generated through evaporation and negative pressure is produced through the condensation such that a pressure difference is produced between the heating and cooling chambers, and wherein the vacuum pump pumps dry air from the cooling chamber as required.

The invention relates to an evaporation dryer (1) for drying particles, having—a process chamber (10) with at least one product inlet (11) for supplying the particles to be dried into the process chamber (10) and a product outlet (12) for discharging dried particles from the process chamber (10), —a heat exchanger (20) arranged within the process chamber (10), —having at least one inlet (21, 211) into the heat exchanger (20) for pressurized steam as process steam and at least one condensate outlet (22, 222) from the heat exchanger (20), wherein—the at least one condensate outlet (22, 222) is connected to an expansion tank (30), wherein at least one pump (40) is connected to the expansion tank (30), and the expanding steam is pumped out of the expansion tank (30) and supplied to the process steam.

An apparatus for drying bulk particulate material, and having an inlet chamber for receiving a moist bulk particulate material and an outlet chamber for ejecting a dry bulk particulate material. The inlet chamber comprises a steam permeable bottom being divided into a number of subsections including a first subsection and a second subsection. Each subsection defines a first and a second radial centreline. The first subsection and the second subsection each having at least one louvered plate section comprising a plurality of louvers arranged in a first and a second specific direction, respectively, for directing superheated steam in a first and second blowing direction, towards said lower cylindrical inner wall. The specific direction of the louvers of the first subsection defines a first angle in relation to the first radial centre-line, and specific direction of said louvers of said second subsection defines a second angle in relation to said second radial centreline, and said first angle and/or said second angle, being different from 0 degrees.

Disclosed is a slurry drying plant (1) comprising a slurry inlet (2) for feeding slurry to the slurry drying plant (1) and two or more meshing screw conveyors (3, 4) arranged to at least partly divide the slurry while conveying the slurry in a transport direction from the slurry inlet (2) to a slurry outlet (5). The slurry drying plant (1) further includes slurry heating means (6) comprising means for passing superheated steam substantially at atmospheric pressure past the slurry and the two or more meshing screw conveyors (3, 4), while they are conveying the slurry. Furthermore, a method for drying slurry and use of a slurry drying plant (1) is disclosed.