DE2029296A1 - (meth)acrylic foams - polymerised and foamed in one operation by heating the monomer in presence of urotropine - Google Patents

(meth)acrylic foams - polymerised and foamed in one operation by heating the monomer in presence of urotropine

Info

Publication number
DE2029296A1
DE2029296A1 DE19702029296 DE2029296A DE2029296A1 DE 2029296 A1 DE2029296 A1 DE 2029296A1 DE 19702029296 DE19702029296 DE 19702029296 DE 2029296 A DE2029296 A DE 2029296A DE 2029296 A1 DE2029296 A1 DE 2029296A1
Authority
DE
Germany
Prior art keywords
meth
opt
urotropine
pref
monomers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
DE19702029296
Other languages
German (de)
Inventor
Wulf von Dr 5090 Leverkusen Bonin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Bayer AG
Original Assignee
Bayer AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Bayer AG filed Critical Bayer AG
Priority to DE19702029296 priority Critical patent/DE2029296A1/en
Publication of DE2029296A1 publication Critical patent/DE2029296A1/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/04Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof using blowing gases generated by a previously added blowing agent
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F20/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
    • C08F20/02Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
    • C08F20/04Acids, Metal salts or ammonium salts thereof
    • C08F20/06Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2333/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

Foams with fine pores and low densities (0.11-0.54 g/cm3) suitable for decorative, insulating or adsorption purposes, also as additives to modify various fillers e.g. mortars, plastics, etc. and also in granular form when hydrophilically modified as soil improvers produced by polymerising and foaming in one operation monomers pref. of (meth)acrylic acid (opt. together with 50% of other olefinic unsat. cpds). in presence of up to equal amts of urotropine (opt. with up to equal amts of other foaming agents, pref. urea) and opt. also of initiators (peroxides, redox systems, pref. N contg. radical donors) at 0.5-5% by heating the monomers with the mentioned additives (opt. also fillers, flame retardants etc) to 30-250 degrees C in moulds or by extruding the mixture through heated jets.

Description

Verfahren zur Herstellung von Schaumstoffen Aufgabe der vorliegenden Erfindung ist ein Verfahren zur Herstellung von Schaumstoffen aus mindestens 50 Gew.-% (Meth)Acrylsäure durch Polymerisation und gleichzeitige Verschäumung0 Die Aufgabe wird dadurch gelöst, daß (Meth)Acrylsäure und gegebenenfalls weitere Monomere in Gegenwart von Urotropin polymerisiert werden.Process for the production of foams Object of the present invention Invention is a process for the production of foams from at least 50 % By weight of (meth) acrylic acid through polymerization and simultaneous foaming 0 Die The object is achieved in that (meth) acrylic acid and optionally other monomers be polymerized in the presence of urotropine.

Gegenstand der Erfindung ist somit ein Verfahren zur Herstellung von Schaumstoffen dadurch gekennzeichnet, daß (Meth)Acrylsäure, gegebenenfalls im Gemisch mit bis zu 50 Gew.-% an anderen olefinisch ungesgttigten Verbindungen thermisch oder in Gegenwart von freie Radikale bildenden Substanzen-in Anwesenheit von Urotropin bei Temperaturen von 30 bis 200°C polymerisiert wird, wobei gleichzeitig Verschäumung erfolgt Die verwendete (Meth)Acrylsäure kann wasserfrei sein bzw.The invention thus provides a method for producing Foams, characterized in that (meth) acrylic acid, optionally in a mixture with up to 50% by weight of other olefinically unsaturated compounds thermally or in the presence of substances which form free radicals - in the presence of urotropine is polymerized at temperatures of 30 to 200 ° C, with simultaneous foaming The (meth) acrylic acid used can be anhydrous or

bis zu 25 Gew.-%, vorzugsweise bis zu 15 Gew.-% an Wasser enthalten, Die (Meth)Acrylsäure kann bis zu 50 Gew.-% durch ein oder mehere Monomere der folgenden Gruppen ersetzt sein: 1.) Ester von α, ß ungesättigten Carbonsäuren mit 3 - 5 C-Atomen im Carbonsäurerest und 1 - 18 C-Atomen in der Alkoholkomponente; vorzugsweise Ester der (Meth)Acrylsäure mit 1 - 8 C-Atomen in der Alkoholkomponente.contain up to 25% by weight, preferably up to 15% by weight, of water, The (meth) acrylic acid can be up to 50% by weight by one or more monomers of the following Groups to be replaced: 1.) Esters of α, ß unsaturated carboxylic acids with 3 - 5 carbon atoms in the carboxylic acid residue and 1 - 18 carbon atoms in the alcohol component; preferably Esters of (meth) acrylic acid with 1 - 8 carbon atoms in the alcohol component.

2.) Amide und Nitrile von α, ß ungesättigten Carbonsäuren mit 3 - 5 C-Atomen, vorzugsweise (Meth)Acrylamid und (Meth)Acrylnitril.2.) Amides and nitriles of α, ß unsaturated carboxylic acids with 3 - 5 carbon atoms, preferably (meth) acrylamide and (meth) acrylonitrile.

3.) Vinylaromaten mit 6 - 10 C-Atomen im Arouatenkern,vorz weise kern- und seitenkettensubstituierte Styrole wie Styrol, α -Methylstyrol, p-Methylstyrol, p-ChlorstyrolO 4.) Ungesättigte Polyester auf Basis von Malein- und/oder Fumarsäureestern.3.) Vinyl aromatics with 6 - 10 carbon atoms in the aromatic core, preferably core and side-chain-substituted styrenes such as styrene, α-methylstyrene, p-methylstyrene, p-ChlorstyrolO 4.) Unsaturated polyesters based on maleic and / or fumaric acid esters.

5.) Vernetzend wirkende Substanzen wie Divinylbenzol, Glykoldi (meth) acrylat, Methylen-bis-(meth)-acrylamid, und zwar in Mengen bis 10 Gew.-%,bezogen auf Gesamtmonomere.5.) Cross-linking substances such as divinylbenzene, glycol di (meth) acrylate, methylene-bis- (meth) -acrylamide, in amounts up to 10% by weight, based on on total monomers.

Bevorzugt werden Acrylsäure und/oder Methacrylsäure ohne Zusatz weiterer Monomerer verwendet. Acrylic acid and / or methacrylic acid without the addition of any other are preferred Monomers used.

Die Polymerisation und gleichzeitige Verschäumung der Monomeren erfolgt bei Temperaturen von 30 bis 2500C , vorzugsweise bei Temperaturen von 50 bis 2000C.The polymerization and simultaneous foaming of the monomers takes place at temperatures from 30 to 2500C, preferably at temperatures from 50 to 2000C.

Die Polymerisation kann thermisch oder durch Zugabe freie Radikale bildender Substanzen ausgelöst werden. Als Radikalbildner seien Peroxide wie tert.-Butylpivalat, tert.-Butyloctoat, Lauroylperoxid, Benzoylperoxid, Cumolhydroperoxid, Di-tert.-Butylperoxid, tert.-Butylhydroperoxid oder Stickstoff enthaltende Radikalbildner wie Azodiisobutyronitril und Derivate genannt. Es können auch Redoxsysteme eingesetzt werden. Bevorzugt werden stickstoffhaltige Radikalbildner wie Azodiisobutyronitril verwendet.The polymerization can be thermal or by adding free radicals forming substances are triggered. Radical generators are peroxides such as tert-butyl pivalate, tert-butyl octoate, lauroyl peroxide, benzoyl peroxide, cumene hydroperoxide, di-tert-butyl peroxide, tert-butyl hydroperoxide or nitrogen-containing radical formers such as azodiisobutyronitrile and called derivatives. Redox systems can also be used. To be favoured nitrogen-containing radical formers such as azodiisobutyronitrile are used.

Die Radikalbildner werden in Mengen von 0,05 bis 15 Gew.-%, bevorzugt in Mengen von 0,5 bis 5 Gew.-%, bezogen auf polymerisierbare Verbindungen, eingesetzt0 Als Verschäumungsmittel, das der Verschäumungsmischung vor der Polymerisation zugesetzt wird, wird Urotropin (Hexamethylentetramin) verwendet. Das Gewichtsverhältnis von Monomeren zu Verschäumungsmittel liegt zwischen 1 : 9 und 9 : 1, bevorzugt zwischen 1 : 3 und 3 : 1.The free radical formers are preferred in amounts of 0.05 to 15% by weight used in amounts of 0.5 to 5% by weight, based on polymerizable compounds0 as Foaming agent added to the foaming mixture prior to polymerization urotropine (hexamethylenetetramine) is used. The weight ratio of Monomers to foaming agent is between 1: 9 and 9: 1, preferably between 1: 3 and 3: 1.

Die Polymerisation und gleichzeitige Verschäumung kann kontinuierlich oder diskontinuierlich erfolgen.The polymerization and simultaneous foaming can be continuous or be carried out discontinuously.

Neben Urotropin als Verschäumungsmittel können gegebenenfalls Harnstoff, Alkylharnstoffe wie Methylharnstoff, Alkylolharnstoff wie Methylolharnstoffe, Cyanamid, Dicyandiamid, Dicyandiamidin, Guanidin in Form seiner Salze, Urethane wie Methylurethan, Ammoniumsalze anorganischer oder vorzugsweise organische Säuren wie Ammoniumnitrat, Ammoniumcarbonat, Ammoniumformiat, Ammoniumoxalat, Ammoniumcarbamat, Ammoniummalemat, Ammoniummaleat sowie Salze organischer und anorganische Säuren von primären Aminen anwesend sein. Vorzugsweise kann Harnstoff neben Urotropin vorhanden sein.In addition to urotropine as a foaming agent, urea, Alkyl ureas such as methyl urea, alkylol urea such as methylol ureas, cyanamide, Dicyandiamide, dicyandiamidine, guanidine in the form of its salts, urethanes such as methyl urethane, Ammonium salts of inorganic or preferably organic acids such as ammonium nitrate, Ammonium carbonate, ammonium formate, ammonium oxalate, ammonium carbamate, ammonium malemate, Ammonium maleate and salts of organic and inorganic acids of primary amines to be present. Preferably, urea can be present in addition to urotropin.

Die Mengen der vorgenannten Zusatzstoffe können bis 100 Gew.-%, bezogen auf Urotropin betragen.The amounts of the aforementioned additives can be up to 100% by weight, based on on urotropine.

Es ist auch möglich, weitere Zusatzstoffe wie flüchtige Lösungsmittel, Füll- und Farbstoffe, Porenregler, flammhemmend, düngend oder biologisch wirkende Hilfsstoffe und dergl. mitzuverwenden.It is also possible to use other additives such as volatile solvents, Fillers and dyes, pore regulators, flame retardant, fertilizing or biologically active To use auxiliary materials and the like.

Im einzelnen kann das Verfahren so durchgeführt werden, daß man Monomere und gegebenenfalls Radikalbildner und weitere Zusatzstoffe gegebenenfalls unter Kühlung innig vermischt, wobei eine Lösung oder ein Brei entsteht.In detail, the process can be carried out in such a way that one monomers and optionally radical formers and other additives, optionally under Cooling intimately mixed to form a solution or a slurry.

Die Verschäumungsmischung kann in eine Form eingebracht werden und die Polymerisation durch kurzzeitiges Erhitzen ausgelöst werden. Während der exthermen Polymerisation erfolgt gleichzeitig die Bildung des Schaumes.The foaming mixture can be introduced into a mold and the polymerization can be triggered by brief heating. During the exthermen Polymerization takes place at the same time as the foam is formed.

Bisweilen neigen frisch hergestellte Mischungen aus den Komponenten, insbesondere bei Verwendung größerer Mengen an Radikalbildnern zu spontaner Selbsterwärmung unter giititigem Aufschäumen.Sometimes freshly made mixtures of the components especially when using larger amounts of radical formers to spontaneous self-heating with good foaming.

Die Polymerisation und gleichzeitige Verschäumung kann auch in einer Presse vorgenommen werden oder während der Extrusion der Mischung durch entsprechend ausgebildete, gegebenenfalls beheizte Düsen erfolgen.The polymerization and simultaneous foaming can also be carried out in one Press or during the extrusion of the mixture through accordingly trained, optionally heated nozzles take place.

Die nach dem Verfahren der Erfindung erhaltenen Schaumstoffe sind schwach gelblich gefärbt, von feinporiger Struktur und besitzen im allgemeinen Raumgewichte unter 0,5g/cm30 Die erhaltenen Schaumstoffe lassen sich zu Flocken zerreißen bzw. in manchen Fällen zu kleinen Teilchen granulieren, in welcher Form sie als Bodenverbesserungsmittel eingesetzt werden können.The foams obtained by the process of the invention are slightly yellowish in color, with a fine-pored structure and generally have bulk weights below 0.5g / cm30 The foams obtained can be torn into flakes or in some cases granulate into small particles, in what form they are used as soil improvers can be used.

Die erfindungsgemäß erhaltenen Schaumstoffe sind zu Dekorations-Isolier- oder Adsorbtionszwecken und neben anderen Verwendungen insbesondere für Zwecke der Bodenverbesserung einsetzbar, da sie sehr leicht hydrophil eingestellt werden können. Sie sind ebenfalls als Zusätze zu anderen Sunststoffen, Kunststoffvorprodukten, Lacken, Mörteln, Vergussmassen, Beton, Ton, Gips usw. geeignet, um deren Eigenschaftsbild zu variieren.The foams obtained according to the invention are used for decorative insulating or adsorption purposes and, in addition to other uses, in particular for purposes of Can be used for soil improvement, as they can be made hydrophilic very easily. They are also used as additives to other plastics, plastic precursors, Paints, mortars, casting compounds, concrete, clay, plaster, etc. are suitable for their property profile to vary.

Die in Beispielen angegebenen Teile beziehen sich auf das Gewicht, sofern nicht anders vermerkt Beispiele 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 Methacrylsäure Tle 1 0,5 0,5 Acrylsäure Tle 1 1 0,5 1 4 2 3 4 0,5 1 1 1 2 0,9 Azodiisobutyronitril Tle 0,05 0,05 0,03 0,02 0,03 0,02 0,03 0,03 0,00 0,05 0,05 0,05 0,05 0,03 Lauroylperoxid Tle 0,02 Urotropin Tle 1 1 2 1 1,5 1,1 1 1 1 1 1 1 1 2 0,5 Harnstoff Tle 1 1 1 1 0,5 0,5 Dicyandiamid Tle 0,5 1 1 Ammoniumformiat Tle 0,5 1 Ammoniumacrytat Tle 1 Methylacrylat Tle 1 Glykoldimethacrylat Tle 0,1 Dichte des Schaumes g/cm³ 0,52 0,3 0,15 0,5 0,45 0,2 0,18 0,11 0,25 0,54 0,33 0,32 0,21 0,35 0,45 Der Versuch nach Beispiel Nr. 10 wird durch Erhitzen der Mischung bis zum Aufschäumen ohne Verwendung eines Radikalbildners durchgeführt, wobei ein thermisch eingeleitete Polymerisationsreaktion ausgelöst wird. Das Mischen der Reaktionspartner in den Beispielen erfolgt wird durch eine auf etwa 75°C erwärmte Düse gepresst, wobei Polymerisatur und Verschäumung (Ausbildung eines Schaumstoffstranges) erfolgt. Der Vorgang verläuft extherm, wobei Temperaturen bis etwa 250°C auftreten können.The parts given in the examples relate to the weight, unless otherwise noted Examples 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 Methacrylic acid part 1 0.5 0.5 Acrylic acid part 1 1 0.5 1 4 2 3 4 0.5 1 1 1 2 0.9 Azodiisobutyronitrile Tle 0.05 0.05 0.03 0.02 0.03 0.02 0.03 0.03 0.00 0.05 0.05 0.05 0.05 0.03 Lauroyl peroxide Tle 0.02 Urotropin Tle 1 1 2 1 1.5 1.1 1 1 1 1 1 1 1 2 0.5 urea part 1 1 1 1 0.5 0.5 dicyandiamide part 0.5 1 1 ammonium formate Part 0.5 1 ammonium acrylate part 1 methyl acrylate part 1 glycol dimethacrylate part 0.1 Density of the foam g / cm³ 0.52 0.3 0.15 0.5 0.45 0.2 0.18 0.11 0.25 0.54 0.33 0.32 0.21 0.35 0.45 The experiment according to example no. 10 is carried out by heating the mixture carried out until foaming without the use of a radical generator, with a thermally initiated polymerization reaction is triggered. Mixing the reactants in the examples it is pressed through a nozzle heated to about 75 ° C, polymerisation and foaming (formation of a foam strand) taking place. The process is extremely thermal and temperatures of up to around 250 ° C can occur.

In dem Beispiel 3 eingesetzte Acrylsäure enthielt 9,5 Gew.-% Wasser.Acrylic acid used in Example 3 contained 9.5% by weight of water.

Claims (1)

PatentansPruch:Patent claim: 1. Verfahren zur Herstellung von Schaumstoffen, d a d u r c h gekennzeichnet, daß (Meth)Acrylsäure, gegebenenfalls im Gemisch mit bis zu 50 Gew.-% an anderen-olefinisch ungesättigten Verbindungen, thermisch oder in Gegenwart von freie Radikale bildenden Substanzen in Anwesenheit voh Urotropin bei Temperaturen von 300 - 2500C polymerisiert wird, wobei gleichzeitig Verschäumung erfolgt.1. Process for the production of foams, d a d u r c h marked, that (meth) acrylic acid, optionally in a mixture with up to 50% by weight of other olefinic acids unsaturated compounds, thermally or in the presence of free radicals Substances polymerized in the presence of Urotropin at temperatures of 300-2500C is, at the same time foaming takes place.
DE19702029296 1970-06-13 1970-06-13 (meth)acrylic foams - polymerised and foamed in one operation by heating the monomer in presence of urotropine Pending DE2029296A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE19702029296 DE2029296A1 (en) 1970-06-13 1970-06-13 (meth)acrylic foams - polymerised and foamed in one operation by heating the monomer in presence of urotropine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19702029296 DE2029296A1 (en) 1970-06-13 1970-06-13 (meth)acrylic foams - polymerised and foamed in one operation by heating the monomer in presence of urotropine

Publications (1)

Publication Number Publication Date
DE2029296A1 true DE2029296A1 (en) 1971-12-23

Family

ID=5773918

Family Applications (1)

Application Number Title Priority Date Filing Date
DE19702029296 Pending DE2029296A1 (en) 1970-06-13 1970-06-13 (meth)acrylic foams - polymerised and foamed in one operation by heating the monomer in presence of urotropine

Country Status (1)

Country Link
DE (1) DE2029296A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3831261A1 (en) * 1988-08-29 1990-03-15 Lentia Gmbh Process for the preparation of liquid-absorbent acrylic resins
DE4344224A1 (en) * 1993-12-23 1995-06-29 Stockhausen Chem Fab Gmbh Crosslinked synthetic polymers with porous structure, high absorption rate for water, aqueous solutions and body fluids, a process for their preparation and their use for the absorption and / or retention of water and / or aqueous liquids

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3831261A1 (en) * 1988-08-29 1990-03-15 Lentia Gmbh Process for the preparation of liquid-absorbent acrylic resins
DE4344224A1 (en) * 1993-12-23 1995-06-29 Stockhausen Chem Fab Gmbh Crosslinked synthetic polymers with porous structure, high absorption rate for water, aqueous solutions and body fluids, a process for their preparation and their use for the absorption and / or retention of water and / or aqueous liquids

Similar Documents

Publication Publication Date Title
DE1258310B (en) Process for producing an embossing effect on a sheet of thermoplastic material
DE1595214C3 (en) Process for the production of thermoplastic polymers which can be foamed by heating
DE1545032A1 (en) Process for the production of block polymers
DE2210837A1 (en) PROCESS FOR THE MANUFACTURING OF SHAPED FOAM BODIES
DE1645264B2 (en) PROCESS FOR THE MANUFACTURING OF MULTIPORE SYNTHETIC POLYMERIZATES
DE1919748A1 (en) Process for the production of foams from ethylene polymers
DE1504674B1 (en) Process for the continuous production of objects from hard foam on the basis of polyvinyl chloride containing polyisocyanates by extrusion
DE69017710T2 (en) METHOD FOR PRODUCING CROSS-LINKED PLASTIC FOAM.
DE2029296A1 (en) (meth)acrylic foams - polymerised and foamed in one operation by heating the monomer in presence of urotropine
DE1569238A1 (en) Process for the production of cross-linked cell bodies on the basis of polyvinyl chloride
DE1645404C3 (en) Process for making a synthetic multicellular resin product
DE2301859A1 (en) PROCESS FOR THE POLYMERIZATION OF ETHYLENIC UNSATURIZED MONOMERS IN FLUID BED
DE2227640A1 (en) Foaming aq silicate solns - using hydrogen peroxide/ reducing agent
DE1301066B (en) Process for the production of multi-pore synthetic polymers
DE2322693A1 (en) Process for the production of elastic flexible foams from olefin polymers
DE102011002905A1 (en) Polyacrylimide foams with reduced content of residual monomers, as well as methods of preparation
DE1249520B (en) Process for the production of foams
DE2123575A1 (en) Plastic compound
AT261918B (en) Process for the production of foams
DE2153532A1 (en) Curing porous silicate foams - which may be used in granular form as soil additives, opt contng pesticides etc
DE1646920C2 (en) Process for improving the strength of fast-setting cements, concretes and mortars
DE2027985A1 (en) Maleic half-ester copolymer foams prodn - using ammonia (source) - as blowing agent have high heat distortion temp
DE1519602C (en) Process for the production of foamable molding compounds from synthetic polyethylene or polypropylene
DE2402441A1 (en) Rapid-setting aminoplast-formaldehyde resin foams - made from mixts contg resin, emulsifier, blowing agent and little water, by adding acids
AT259864B (en) Process for continuous bulk polymerization