GB768049A - Production of natural or artificial rubber and other elastomers - Google Patents

Production of natural or artificial rubber and other elastomers

Info

Publication number
GB768049A
GB768049A GB36355/54A GB3635554A GB768049A GB 768049 A GB768049 A GB 768049A GB 36355/54 A GB36355/54 A GB 36355/54A GB 3635554 A GB3635554 A GB 3635554A GB 768049 A GB768049 A GB 768049A
Authority
GB
United Kingdom
Prior art keywords
oxides
aluminium
mixture
silicon
flame
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.)
Expired
Application number
GB36355/54A
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.)
Evonik Operations GmbH
Original Assignee
Degussa GmbH
Deutsche Gold und Silber Scheideanstalt
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 Degussa GmbH, Deutsche Gold und Silber Scheideanstalt filed Critical Degussa GmbH
Publication of GB768049A publication Critical patent/GB768049A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals

Abstract

A mixture of oxide-forming volatile metal and/or metalloid compounds is homogeneously mixed with a free oxygen-containing gas and a combustible gas and the mixture fed to a burner and reacted in the flame to form mixed or combined or partially combined oxides suitable for use as a filler for natural and synthetic rubber and other elastomers. The proportions of the constituents of the homogeneous mixture are preferably stoichiometric for the formation of the oxides and complete combustion of the combustible gas. A suitable combustible gas is carbon monoxide or, to produce a more rapid reaction and finer particles, hydrogen or gas mixtures or gases which contain or yield hydrogen (e.g. methane or illuminating gas) and thus result in the production of water in situ. In order to reduce the particle size the dilution of the oxide-forming compounds may be increased, e.g. by increasing the proportion of oxygen-containing gas such as air and, to avoid reduction in throughput, increasing the input velocity. It is preferred to use as low a flame temperature as possible, e.g. 900 to 1200 DEG C., to avoid healing and eliminating lattice faults in the oxides, by regulating the amount of combustible gas or by supplying an inert gas such as nitrogen to the flame. The latter expedient also reduces the particle size. Similarly a short time of stay in the flame is desirable and this may be achieved by the use of large but short flames, e.g. as produced by a sprinkler type of burner illustrated in Specification 726,250. The mixture is preferably supplied to the flame in laminer flow (as described in the above Specification) to promote homogeneous distribution therein, and to avoid deposition on the rim of the burner, washing gases such as air or hydrogen, or mechanical stripping may be employed. To promote the formation of a favourable product, the aerosol resulting from the reaction is preferably allowed to condense to an aerogel in the presence of previously coagulated particles, and to this end a long path of travel and vigorous movement of the aerosol is desirable, e.g. by whirling in large chambers or movement through long tubes with several bends to keep the particles in suspension until coagulation takes place, e.g. for 3, preferably 5 seconds, before separation in cyclones. Specified volatile compounds are the halides, especially chlorides, of silicon, aluminium, titanium, zirconium, iron and chromium; organometallic compounds such as aluminium ethyl, silicon tetra-ethyl, silicon tetramethyl and trichlorosilane; mixtures referred to are silicon tetrachloride and aluminium chloride (to form a substance which is the preliminary stage of an aluminium silicate), the aluminium chloride preferably being present as 0.5 to 30 per cent by weight of the mixture, silicon and titanium tetrachlorides, the latter being present to the extent of 5 to 35 per cent by weight of the mixture; fillers consisting of titanium and aluminium oxides, zirconium and aluminium oxides, or said oxides with iron, chromium or vanadium oxides are mentioned.ALSO:Rubber is made up into a mix with a filler produced by homogeneously mixing a mixture of oxide-forming volatile metal and/or metalloid compounds with a free oxygen-containing gas and a combustible gas, feeding the homogeneous mixture to a burner and reacting the mixture in a flame (see Group III). The products, which may be mixed or combined or partially combined oxides are preferably in the form of aerogels and may have been obtained from the halides (silicon, aluminium, titanium, zirconium, iron and chromium chlorides) or organometallic compounds (aluminium ethyl, silicon tetra-ethyl, silicon tetra-methyl and trichlorosilane) of the metal or metalloids, and and specific mixtures referred to are silicon tetrachloride and aluminium chloride, (to form a substance which is the preliminary stage of an aluminium silicate) and silicon and titanium tetrachlorides; fillers consisting of titanium and aluminium oxides, zirconium and aluminium oxides or said oxides with iron, chromium or vanadium oxides are mentioned. In examples, (1) 40 parts of 10 per cent alumina, 90 per cent silica filler and 100 parts of rubber were vulcanized and (2) a mixture as in (1) and containing also stearic acid (1 part) Ozokerite (2,7 parts) zinc oxide (5 parts) "Vulcazit" (Registered Trade Mark) accelerator (2,5 parts) and sulphur (4,0 parts) was vulcanized. Specification 726,250 [Group III] is referred to.
GB36355/54A 1953-12-15 1954-12-15 Production of natural or artificial rubber and other elastomers Expired GB768049A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE768049X 1953-12-15

Publications (1)

Publication Number Publication Date
GB768049A true GB768049A (en) 1957-02-13

Family

ID=6673595

Family Applications (1)

Application Number Title Priority Date Filing Date
GB36355/54A Expired GB768049A (en) 1953-12-15 1954-12-15 Production of natural or artificial rubber and other elastomers

Country Status (2)

Country Link
BE (1) BE534117A (en)
GB (1) GB768049A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2360288A (en) * 2000-03-10 2001-09-19 Goodyear Tire & Rubber Pneumatic tire having a tread containing a metal oxide aerogel
US6527022B2 (en) 2000-03-10 2003-03-04 The Goodyear Tire & Rubber Company Pneumatic tire having a tread containing a metal oxide aerogel

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2360288A (en) * 2000-03-10 2001-09-19 Goodyear Tire & Rubber Pneumatic tire having a tread containing a metal oxide aerogel
US6527022B2 (en) 2000-03-10 2003-03-04 The Goodyear Tire & Rubber Company Pneumatic tire having a tread containing a metal oxide aerogel
GB2360288B (en) * 2000-03-10 2003-12-03 Goodyear Tire & Rubber Pneumatic tire having a tread containing a metal oxide aerogel

Also Published As

Publication number Publication date
BE534117A (en)

Similar Documents

Publication Publication Date Title
US4276274A (en) Process for the production of finely divided oxides of metals or silicon
US3954945A (en) Process for the production of finely divided oxides
US2819151A (en) Process for burning silicon fluorides to form silica
US3660132A (en) Process of making a highly dispersed mixture of carbon black and silicic acid
US4211578A (en) Method of producing a carbon black silica pigment
US2990249A (en) Process of preparing finely divided oxides by hydrolysis
KR880000325A (en) Chlorine Production Method
US2980509A (en) Vapor phase process for the production of titanium dioxide
KR20050074289A (en) Silicon-titanium mixed oxide powder produced by flame hydrolysis
US3214284A (en) Production of pigmentary titanium oxide
US4755371A (en) Method for producing carbon black
CA1179477A (en) Process for the controlled production of silica by means of flame hydrolysis
US5372795A (en) Process for hydrophobicizing of pyrogenic silica
US3416890A (en) Process of producing oxides of metals and metalloids
JPS6015569B2 (en) Equipment for pyrolytically producing silicon dioxide
GB768049A (en) Production of natural or artificial rubber and other elastomers
US3723611A (en) Production of chromium (iii) oxide of low sulfur content
US2847316A (en) Process for production of mixed metal oxides
GB2037266A (en) Vapour phase oxidation of titanium tetrachloride
US2437171A (en) Composite titanium dioxide-metal oxide pigment
US6322765B1 (en) Process for preparing silicon dioxide
US3795731A (en) Process for the combustion of ammonium sulfate
US3036926A (en) Process for improving titanium dioxide pigments
US3661522A (en) Process for producing pigment grade titanium dioxide
JP2889202B2 (en) Method for producing highly dispersible silicon dioxide