Abstract:
The present invention relates to a porous inorganic body comprising pores A having a pore size SA in the range of from 0.005 to 20 micrometer and a total pore volume VA, and comprising pores B having a pore size SB in the range of from more than 20 to 1000 micrometer and a total pore volume VB, wherein the total pore volume of the pores having a pore size in the range of from 0.005 to 1000 micrometer is VC and wherein the ratio RA = VA / VC is in the range of from 0.3 to 0.7 as determined via mercury intrusion porosimetry.
Abstract translation:本发明涉及一种多孔无机体,其包含孔尺寸SA在0.005至20微米范围内的孔A和总孔体积VA,并且包含孔径SB在大于20的范围内的孔B 至1000微米和总孔体积VB,其中孔径在0.005至1000微米范围内的孔的总孔体积为VC,其中RA = VA / VC的比率在0.3至 0.7通过汞侵入孔隙率法测定。
Abstract:
A process for the production of insecticide-modified bead material composed of expandable polystyrene (EPS) by extrusion, encompassing the steps of a) mixing, in a mixer, to incorporate a blowing agent and at least one insecticide from the group of the phenylpyrazoles, chlorfenapyr and hydramethylnon into a polymer melt which comprises at least one polystyrene, based on a vinylaromatic monomer, b) discharging the polymer melt comprising blowing agent, and c) pelletizing the polymer melt comprising blowing agent.
Abstract:
The invention relates to a device for extruding moulding compounds, comprising at least two worms (1) received in a housing (3). Said device has at least one feed section, one transformation section and one discharge section, which can at least partially overlap each other, and at least one degassing opening (5). The degassing opening (5) creates a partial region in the housing (3) over at least two worms (1) engaging in each other. A section (9) is formed in the degassing opening (5) in the engaging region (11) of each worm (1). A gap (13) is formed between the section (9) and the at least one worm (1a) rotating in the region of the degassing opening (5) towards the section (9), the width of the gap decreasing in the direction of rotation of the worm (1a).
Abstract:
The invention relates to a method for producing thermoplastic molding compounds, comprising: A) 40 to 99 wt % of at least one thermoplastic polymer, B) 1 to 60 wt % of a flame-proofing agent component containing an expandable graphite, and C) 0 to 60 wt % of further additives, by melt-mixing components A), B) and C) in a screw-type extruder, wherein the screw-type extruder, along the feed direction, comprises, in the following order, at least one dosing zone, a plastifying zone, a homogenizing zone, a second dosing zone, and a discharge zone, in that the dosing takes place into the screw-type extruder having the length L, wherein the length L is defined as the section starting with the first dosing unit for adding components A, B and/or C and ending, in the feed direction, at the discharge opening, a melt is generated after adding components A, B and C in the range of 0 liter to 0.15 liter in a first method step in the presence of component B1), and in a second method step, after the addition of component B1) in the range of 0.5 liter to 0.95 liter, component B1) is mixed into said melt, wherein said method offers technical advantages.
Abstract:
Insecticide-modified bead material composed of expandable polystyrene (EPS), comprising at least one insecticide selected from the group of the insecticidal phenylpyrazoles, chlorfenapyr and hydramethylnon which is distributed in molecular dispersion in the polystyrene matrix.
Abstract:
A mixture comprising a) 5 to 95 wt.-% of a copolymer A that contains one or more copolymer blocks (B/S)A, each made of 65 to 95 wt.-% of vinyl aromatic monomers and 5 to 35 wt.-% dienes and having a glass transition temperature Tg A in the range of 40° to 90°C, b) 5 to 95 wt.-% of a block copolymer B containing at least one hard block S made of 95 to 100 wt.-% of vi-nyl aromatic monomers and 0 to 5 wt.-% dienes, one or more copolymer blocks (B/S)A, each made of 65 to 95 wt.-% of vinyl aro-matic monomers and 5 to 35 wt.-% dienes and having a glass transition temperature Tg A in the range of 40° to 90°C and one or more copolymer blocks (B/S)B, each made of 20 to 60 wt.-% of vinyl aromatic monomers and 40 to 80 wt.-% dienes and having a glass transition temperature Tg B in the range of -70° to 0°C, c) 0 to 45 wt.% of A and B of various thermoplastic polymers C and d) 0 to 6 wt.-% of processing aids D, wherein the total of A through D is 100 wt.-%, and use thereof for the production of shrink--wrap films.
Abstract:
Masas de moldeo termoplásticas que contienen los siguientes componentes: (A) del 15 al 80 % en peso de por lo menos un poliarilen-éter, (B) del 5 al 70 % en peso de por lo menos un poli(sulfuro de arileno), (C) del 0 al 15 % en peso de por lo menos un poliarilen-éter funcionalizado que comprende grupos carboxilo, (D) del 15 al 70 % en peso de por lo menos una carga en forma de fibra o en forma de partícula y (E) del 0 al 40 % en peso de aditivos adicionales y/o agentes auxiliares de procesamiento, ascendiendo la relación de la viscosidad aparente del componente (A) con respecto a la del componente (B) a de 2,5a 3,7, determinándose la viscosidad aparente a 350 ºC y a una tasa de cizalladura de 1150 s-1 con un viscosímetrocapilar con un capilar circular de 30 mm de longitud, un radio de 0,5 mm, un ángulo de entrada de la boquilla de180º, un diámetro del recipiente de depósito de la masa fundida de 12 mm y con un tiempo de precalentamiento de 5minutos y ascendiendo la suma de los % en peso del componente (A) a (E) al 100 % en peso.
Abstract:
Intercambiador de calor de haz tubular para la separación de sustancias volátiles de una disolución poliméricamediante desgasificación, que comprende en un espacio revestido atravesado por un portador de calor fluido un hazde tubos dispuestos de manera paralela uno con respecto a otro y de manera vertical, donde los tubos están fijadosrespectivamente con su extremo superior en una base de tubo superior y con su extremo inferior en una base detubo inferior y se atraviesan por la disolución polimérica que va a desgasificarse en dirección de la fuerza de lagravedad, caracterizado por que en el lado superior de la base de tubo superior está colocada una tela de alambrede varias capas, cuya capa de malla más fina presenta un ancho de malla de 50 μm a 1000 μm.
Abstract:
Process for producing cellulose beads or lignocellulose beads, wherein cellulose or lignocellulose is dissolved in a solvent which comprises more than 50% by weight of the symmetrical imidazolium compound of the formula I below where R1 and R3 are each an identical organic radical having from 2 to 20 carbon atoms, R2, R4 and R5 are each an H atom, X is an anion and n is 1, 2 or 3, and cellulose beads or lignocellulose beads are produced from the solution obtained, and also the use of the beads obtained for petroleum or natural gas recovery.