Classifications

• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
• • C—CHEMISTRY; METALLURGY
  • C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
  • C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
  • C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
  • C04B18/02—Agglomerated materials, e.g. artificial aggregates

Definitions

• the invention relates to a method for producing a finely divided powder containing thermoplastic material.
• thermoplastic plastics which takes the form of pieces, granules, chips, grains and the like.
• comminution machines such as cutting units, shredders and mills
• the energy to be used for further fragmentation also rises sharply, so that even with a relatively large amount of energy and the use of powerful machines, a very slow progress in reducing the particle size can soon be achieved. All of this is disadvantageous if larger amounts of a finely divided powder are to be produced from a thermoplastic material which is in a much coarser form.
• thermoplastic material is introduced into a non-aqueous carrier substance, in particular bitumen, which is liquid in the melting temperature range of the plastics material, and in this melting temperature range with the carrier substance to form an, at least visually, homogeneous mass is mixed that ground this mass Quicklime is added and distributed in the mass, that an aqueous sludge is then added to the mass and distributed in the mass, and the mass is converted into a plastic-containing powder by the resulting reaction between the quicklime and the aqueous sludge.
• a non-aqueous carrier substance in particular bitumen
• the above-mentioned objective can be met very well and a powder which contains thermoplastic plastic in a very finely divided form is obtained in a simple manner with a relatively fast process sequence. It can be carried out with little expenditure on equipment and with low expenditure of energy.
• the carrier substance is heated to a temperature in the range of the plastic material before the plastic material is introduced.
• the mixing of the plastic material with the carrier substance can be carried out quickly and easily and the required heating of the plastic material in the melting temperature range can be accomplished in a very short time in this way.
• the mass ratio of carrier substance to plastic material is selected between 1: 5 and 10: 1.
• easy mixing of the quicklime into the mass containing the carrier substance and the plastic material is of great importance and it is advantageous in the sense of a simple and rapid implementation of this process step, provided that that the mass consisting of the carrier substance and the plastic material or the carrier substance before the addition of the plastic material as an oil or organic solvent forming a solution with the carrier substance or the mass, the boiling point of which is 10 to 20 ° C. lower than the decomposition temperature ⁇ temperature of the plastic material used, is added.
• this oil or solvent can be left in the reaction mass.
• thermal expulsion in particular distillation
• an organic solvent has been added Recommended procedure.
• Such expulsion or distillation can advantageously be carried out using the heat generated during the reaction of the quicklime with the aqueous sludge or the heating of the mass caused thereby; the solvent distilled off is expediently circulated in order to make the process particularly economical.
• Decalin and tetralin in particular can advantageously be used as solvents in the pulverization of polyethylene.
• a quicklime ground to a grain size of less than 0.1 mm is used in the process according to the invention.
• highly reactive, soft-fired quicklime is used in the process according to the invention.
• the mass ratio of the mass containing the carrier substance and the plastic material and calculated without oil or solvent to quicklime is between 1: 2.5 and 1: 3.5, preferably 1: 2.8 to 1: 3, chosen x ⁇ ird.
• the amount of water provided for reaction with the quicklime is " ""' " it is advantageous if the mass is cooled to a temperature of around 100 ° C. before the aqueous sludge is added.
• the solid of the aqueous sludge remains in the end product of the process, it is generally favorable for the further processing of the end product if an aqueous sludge containing an inorganic material is used as a solid. It is primarily important that the solid of the aqueous sludge containing the reaction water for the reaction with the quicklime has a sufficiently large porosity and that it does not interfere with the later use of the plastic-containing powder; it comes in handy
• a particularly advantageous embodiment of the method according to the invention provides for the use of red mud, which is obtained as a waste product in the production of aluminum, with regard to the aqueous sludge.
• red mud is available cheaply and is already obtained in the water-saturated state, so that it no longer has to be processed, and also has a relatively high porosity, so that with a relatively small amount of sludge this is necessary for the reaction with the Quicklime required reaction water can be supplied.
• the amount of sludge used is selected so that the ratio of the mass of the water contained in the sludge to the mass of the quicklime is between 1: 1.8 and 1: 2, preferably 1: 1.9.
• the aqueous sludge before it is added to the mass containing the plastic material, the carrier substance and the quicklime, to a temperature above 75 ° C., preferably to about 90 ° C, lying temperature is heated.
• the procedure is advantageously such that the aqueous sludge is first applied to the surface of the mass and distributed over it and then rapidly stirred into the mass.
• the process according to the invention offers particular advantages for the production of powders which contain polyolefins, in particular polyethylene, as plastic.
• bitumen preferably provided as the carrier substance in the method according to the invention is very favorable.
• other substances can also be used as carriers, e.g. Hard paraffin, fats and waxes, if the properties of the bitumen, which is also present in the finished powder, would interfere with the later use of the powder.
• thermoplastic material for producing a finely divided powder containing thermoplastic material
• Example A 10 parts by weight of bitumen were heated in a heatable vessel to a temperature of about 200 ° C. and 20 parts by weight of coarsely divided polyethylene waste were introduced into this melted, thin bituminous bitumen mass, and the resulting mixture was stirred mixed until there was a visually homogeneous mass. In this way, a slightly pasty, bright melt was obtained.
• This melt was diluted by adding 40 parts by mass of decalin. 84 parts by weight of finely ground quicklime with a particle size of less than 0.1 mm were stirred into the now relatively thin liquid mass obtained in this way. A highly reactive soft brandy quicklime was used.
• the mass was cooled to a temperature of approximately 100 ° C.
• This mass was then mixed with 100 parts by mass of red mud, which is a waste product from aluminum production and has a water content of approximately 40 to 50% by mass, this red mud was first preheated to 90 ° C., then onto the surface of the carrier substance, the plastic material and the Mass containing quicklime was applied and distributed over the surface and was then mixed with this mass by rapid and intensive stirring.
• a sudden use of the reaction of the water contained in the red mud with the quicklime present in the mass was achieved. In this reaction, the quicklime was converted to calcium hydroxide with the water of reaction and a fine free-flowing powder was formed from the entire mass by this reaction.
• Example B The procedure was analogous to that in Example A and initially 20 parts by weight of bitumen were heated to about 200 ° C. 50 parts by weight of polyethylene in divided form were introduced into this hot bitumen mass and the mixture was mixed until visually homogeneous. 100 parts by weight of decalin were then added, and 210 parts by weight of quicklime were then stirred in, and the mixture was then cooled to a temperature of about 100.degree. This mass was then mixed with a mixture previously formed from 180 parts by mass of fly ash and 90 parts by mass of water, which was first carefully layered onto the bitumen-plastic-lime mass and then quickly stirred in. In the reaction that followed, a fine, free-flowing powder was formed from the entire mass.
• the invention further relates to a method for producing a bituminous bound building material, in particular road building material, which contains a grain-graded aggregate consisting of filler, sand and grit or gravel and a binding agent and its binder with thermoplastic ⁇ chemical plastic, in particular a polyolefin, such as polyethylene, is added.
• a bituminous bound building material in particular road building material, which contains a grain-graded aggregate consisting of filler, sand and grit or gravel and a binding agent and its binder with thermoplastic ⁇ chemical plastic, in particular a polyolefin, such as polyethylene, is added.
• This method according to the invention is characterized in that the plastic in the form of finely divided particles which mixes with an inorganic material corresponding to a filler in particle size or is attached to these particles. are stored, is added, the plastic preferably being added in the form of a powder containing plastic obtained by a process according to the invention as described above.
• the plastic provided for modifying the binder properties of the bitumen can be introduced into the building material in a simple manner without the aid of special devices, and a very effective modification of the binder can be achieved in relation to the amount of plastic used.
• This procedure according to the invention can also have disadvantages which occur in known techniques for the plastic coating of bitumen used as a binder, such as Demixing phenomena of the pair of materials bitumen-plastic, practically be switched off.
• An embodiment of the method according to the invention is particularly advantageous, which is characterized in that the plastic is added in the course of the mixing process in which the aggregate is combined with the bitumen to form the building material.
• the powder containing the plastic can advantageously be introduced into the mixture consisting of a bituminous binder and the aggregate using the technique which is normally used for adding the so-called filler.
• plastic with a particle size of less than 0.09 mm is used. It is also advantageous for the introduction of polyethylene as plastic into the binder of the bituminous building material if one provides that a ratio of the mass of the plastic to the mass of the inorganic material, with that of the plastic
• Material mixed or to which it is attached, is provided from about 1: 7.5.
• rock or sand material with a sieve line standardized for asphalt concrete 0/18 was preheated to approx. 170 to 180 ° C in an asphalt mixer and bitumen B100, which also has a temperature of approx. 170 to 180 ° C had injected into the mixer.
• the mixer was filled with limestone powder as a filler and further also powder containing plastic, which had previously been produced according to Example A or Example B.
• Several masses intended for use as road building material were produced in succession, which differed from one another in terms of the amount of addition of plastic-containing powder.
• the amount of the binder based on the total amount of the building material mass, to which the bitumen B100 and the plastic portion of the plastic-containing powder is to be counted, was kept constant at 5.1 mass for all masses.
• the same amount and composition of the aggregate (rock or sand material, filler) were provided for all the masses, and the same (standardly provided) amount of filler was added, the mineral content of the plastic-containing powder also being added to the filler was calculated and the bitumen content of the plastic-containing powder was also taken into account by a corresponding reduction in the bitumen used to form the respective binder.
• the modulus of elasticity which can be calculated from the examinations carried out on the Marshall bodies has a progressively increasing course with increasing polyethylene content and this can be described by an axial function.
• the road building materials produced according to example group 3 for comparison shows an increasing gap tensile strength with increasing polyethylene content, whereby the dependence of the splitting tensile strength on the polyethylene content in the area under consideration can be described by an increasing saturation function.
• the upsetting of the road building materials produced according to example group 3 increases, as from those that represent the upsetting
• Curves 4a and 4b can be seen, similar to the compression of the road building materials according to example group 2, slowly with increasing polyethylene content.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Civil Engineering (AREA)
• Materials Engineering (AREA)
• Structural Engineering (AREA)
• Ceramic Engineering (AREA)
• Organic Chemistry (AREA)
• Polymers & Plastics (AREA)
• Medicinal Chemistry (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Health & Medical Sciences (AREA)
• Compositions Of Macromolecular Compounds (AREA)
• Road Paving Structures (AREA)
• Processes Of Treating Macromolecular Substances (AREA)
• Soil Conditioners And Soil-Stabilizing Materials (AREA)
• Medicinal Preparation (AREA)

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• 1983
  • 1983-02-22 AT AT0060983A patent/AT383823B/de not_active IP Right Cessation
• 1984
  • 1984-02-20 DD DD84260196A patent/DD224312A5/de not_active IP Right Cessation
  • 1984-02-20 CA CA000447828A patent/CA1214893A/en not_active Expired
  • 1984-02-21 EP EP84900835A patent/EP0163649A1/de active Pending
  • 1984-02-21 EP EP84890032A patent/EP0119985A1/de not_active Withdrawn
  • 1984-02-21 JP JP59500954A patent/JPS60500624A/ja active Pending
  • 1984-02-21 ES ES529899A patent/ES529899A0/es active Granted
  • 1984-02-21 HU HU841075A patent/HU195672B/hu not_active IP Right Cessation
  • 1984-02-21 WO PCT/AT1984/000009 patent/WO1984003294A1/de not_active Application Discontinuation
  • 1984-02-21 BR BR8406985A patent/BR8406985A/pt unknown
  • 1984-10-05 DK DK478084A patent/DK478084D0/da not_active Application Discontinuation
  • 1984-10-19 NO NO844182A patent/NO844182L/no unknown
• 1985
  • 1985-03-22 FI FI851157A patent/FI851157L/fi not_active Application Discontinuation
  • 1985-08-09 US US06/764,232 patent/US4617201A/en not_active Expired - Fee Related

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