DE1461425C - Apparatus for recovering particulate polymer solids from a slurry - Google Patents

Description

3 4

the substances vorgenom in a single device is filtered through the filter membrane 3, namely

men will be. depending on the type of polymer and the carrying fluid

The slurry from the carrying fluid and under the action of the pressure of the inlet

The polymer usually consists mainly of nozzle 5 or steam introduced into the vessel

the carrying fluid, d. H. from a liquid portion 5 under the action of gravity. The carrying liquid flows

in an order of magnitude of 60 to 90 weight via the outlet nozzle 4 and is back-

percent, and a polymer content in one size. The polymer material remains on the

Order of 40 to 10 percent by weight. Usually filter membrane lie. The pressure treatment with

a weight ratio of 80% liquid vapor continues until the vapor is total

and 20% polymer used. The invention has stripped the carrying fluid from the polymers. Ever

However, proper device may work with success depending on which aperture is used

Slurry can be used which flows 10 to 95% steam either downwards or upwards.

Contains carrying fluid. During the whole process it rotates

For conveying the granular polymer, stirrer 6 is used at a very low speed of preferably inert gas, for example nitrogen, for example 1 to 20 rpm, which turns the polymer. However, one can generally use any gas mass in the granular state, since it does not affect the quality of the polymer polymer lump on the impact bars 7 and does not affect the polymer when the carrying fluid reacts completely from the poly itself. For example, air can be scraped off and turn it relatively dry. Depending on the moisture content of the 20, a vacuum is applied to the polymer cake and the required lifting height via the vacuum nozzle 8 and a rapid and conveying section takes place, this step under an evaporation of water to the moisture pressure of about 0.07 carried out to about 3.5 atmospheres. You can go above or below. _v half of the polymer a vacuum to act

The invention will bring about an embodiment 25 or the polymer with hot inert gases

explained in more detail on the basis of the drawing. dry. Then via the inlet connection 9 a

The device consists of a "container 2", pressurized gas is introduced into the vessel and the material

the through a filter membrane 3 in an upper first via "the" tube 10 to the next process step

and a lower second chamber is divided. In the upper part fed in, in which the polymer is further compressed

Part of the first chamber is an entry 30 and then pelletized.

opening 1 for the suspension to be dispensed and a The device according to the invention is with polymer nozzle 5, through which steam is introduced. Can be used in slurries, e.g. B. by upper part of the second chamber are a vacuum suspension polymerization using high nozzle 8, an inlet nozzle 9 for a conveying gas pressures can be obtained. She is particularly used to and in its bottom an outlet 4 for the separation of suspensions suitable for the low-filtrate appropriate. In the first chamber there is pressure according to Ziegler or Phillips, with help a stirrer 6, which can be obtained with its stirring rods from catalysts. However, it can the baffle rods 7 sitting in the filter base were moved past - with unusually good success also to the tren. From the top of the first chamber protrudes from another polymer from slurries pipe 10 at a sufficient distance from the filter base 40 can be used. For example, it can be reduced through which the polymer parts from the supply for the production of polystyrene, polybutylene, direction to be promoted. Polyisoprene, polyvinyl chloride, polyvinyl acetate, poly-

Use those from the carrier liquid and the polymers acetate and other polymers that are in

existing slurry is converted into a slurry or suspension process via the entry process

opening 1 introduced into container 2 until a generated 45 including copolymers,

the correct level has been reached. The carrier fluid such as polyethylene propylene.

1 sheet of drawings

Claims (1)

1 ■■ '■■ · ■ ·.;,; 2. "'■ - usually by extrusion. Then the patent claim: Polymers is transferred to a: Packaging device ■. . give. : Device for obtaining granular In the Ziegler process and in other Polymer solids from a slurry 5 drive to the production of olefin polymers is the the solids in a carrier liquid, the best separation and recovery of the solid polymers Starting from one through a filter base into two "liquid" mixtures containing these are difficult Compartments divided, closed containers, and expensive. The polymer particles strive to each other its first, located above the filter base, to adhere and to agglomerates or polymer lumps Chamber form an inlet opening for the slurry, especially while the liquid is demineralized as well as a stirring device, is removed. This will further processing while the second chamber severely obstructs an outlet opening of the polymer. The agglomerates for the, liquid phase or an inlet opening or. Lumps also contain solvents for a gaseous medium possesses g e k e η η - inclusions caused by the action of heat or by is not readily characterized by wiping into the second chamber 15 with an inert gas (15) opening inlet nozzle (9) can be removed for one. Besides that, it can Conveying gas and a polymer sticky in the first chamber (14) from which the liquid is removed protruding pipe (10) for discharging which has been, not without difficulty to the pre-solids be conveyed by the conveying gas as well as by devices that are used for compression known to serve in the first and second chamber ao and pelletization of the polymer. For the confluent inlet and outlet nozzles (5 avoidance of lump formation, the removal or 8) for a drying medium. . of inclusions of the carrier medium and one. easy removal of the solids from the separation device for further processing are the '- »5 conventional separating devices not suitable. '- ■. . U.S. Patent 2,404,215 is a Vor described direction for filtering sludge, The invention relates to a device whose solid parts have different sizes. Obtaining granular polymer solids from This consists of a closed container that a slurry of the solids in a carrier 30 divided into two chambers by a filter bottom liquid consisting of a through a filter is. For the introduction of the slurry is in the bottom divided into two chambers, closed chamber located above the filter bottom a single container, the first chamber of which an inlet opening is provided. Located in this chamber for the slurry and a stirring device, there is a stirring device. The bottom of the lower has, while the second chamber has an outlet 35 chamber has an opening which can optionally be used for Opening for the liquid phase or an entry withdrawal of the liquid phase or for admission Has opening for a gaseous medium. . one to loosen up the slurry - Many polymers are used in the form of granules for the air flow. The filter cake obtained from the liquid, which is suspended in a liquid medium, is largely separated off, from which the granular polymer is separated and an area provided near the filter membrane must then be dried until all the liquid is drawn off as a slurry,
is removed so that the polymer is present in a form suitable for this known device insofar as it can be used further. part than one for drying the filtered material A group of very valuable polymers that require separate drying equipment what can be obtained in the form of a slurry, 45 associated with an increased structural effort i.e. in the form of a granular solid which is in. . a liquid is suspended, the solid The invention is therefore based on the object Olefin polymers, especially ethylene and pro a .Vorrichtung for separating lumpy pylenpolpolymers, which in many Polymerisationsverfah-. '■■ ' or sticky polymer solids from a rupture at any point in the process. To create 50 slurry in a carrier liquid, polyolefins, in particular polyethylene and co- with which it is possible to strip the polymers in a single polymer of ethylene and other copolymerizing device and in one operation by filtering, bare monomers, are stripping and in certain processes To gain drying and to discharge _{from the} device under high pressures and at high temperatures. ',.;
generated in the form of a slurry. The task in an apparatus for slurrying the polymer is of a type mentioned at the beginning according to the invention through the into an extruder, in which one of the inlet polymers opening into the second chamber is compressed and the Carrier medium opening for a conveying gas and a pressurized into the first and removed. Difficulties arise in this case, the tube protruding into the chamber for discharging the solids with regard to the removal of the carrier medium through the conveying gas and through the polymer itself. Known, in the first or second chamber In the polymerization process according to Ziegler, opening and outlet openings for a on which the invention is solved with particular advantage on drying medium. is reversible, the insoluble polymer is by this embodiment of the invention Carrying liquid by filtration, centrifugation or 65 device can all be used to obtain the other suitable physical separation processes - polymer solids not separated from a slurry. ' After drying, the polymer must be manoeuvrable process measures including the compacted and pelletized. This takes place in an almost carrier-free state.