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76results about How to "Improve machining productivity" patented technology

Continuous and semi-continuous process of manufacturing titanium hydride using titanium chlorides of different valency

InactiveUS20110171116A1Reduce manufacturing costCost-effective and highly-productive manufactureTransition element hydridesTitanium chlorideOxygen
The invention relates to the manufacture of titanium hydride powder using continuous or semi-continuous process, and using titanium slag or synthetic rutile as raw materials, while hydrogen, titanium tetrachloride, titanium trichloride, titanium dichloride, and hydrogen chloride are participate as intermediate reaction products. The continuous comprises: (a) reduction of TiCl4 to low titanium chlorides followed by cooling a mixture, (b) separating of residual TiCl4 from solid low chlorides by heating the mixture in argon or vacuum up to 150° C. followed by removing the titanium tetrachloride from the mixture, (c) dissociation of TiCl3 to TiCl2 at 450° C. in vacuum followed by removal of gaseous titanium tetrachloride from the reaction zone, condensation to the liquid, and returning back into the reaction retort, (d) dissociation of TiCl2 in vacuum at 750-850° C. to manufacture fine powder of metallic titanium and titanium tetrachloride, whereby hydrogen heated up to 1000° C. is used to accelerate this reaction, and (e) saturation of the fine titanium powder by hydrogen at 400-640° C. to manufacture final product of titanium hydride powder which is free of oxygen or nitrogen. The semi-continuous process includes the Kroll's process as the very first step.
Owner:ADMA PRODS

Continuous and semi-continuous process of manufacturing titanium hydride using titanium chlorides of different valency

InactiveUS8388727B2Cost-effective and highly-productive manufactureImprove machining productivityTransition element hydridesTitanium chlorideTitanium(II) chloride
The invention relates to the manufacture of titanium hydride powder using continuous or semi-continuous process, and using titanium slag or synthetic rutile as raw materials, while hydrogen, titanium tetrachloride, titanium trichloride, titanium dichloride, and hydrogen chloride are participate as intermediate reaction products. The continuous comprises: (a) reduction of TiCl4 to low titanium chlorides followed by cooling a mixture, (b) separating of residual TiCl4 from solid low chlorides by heating the mixture in argon or vacuum up to 150° C. followed by removing the titanium tetrachloride from the mixture, (c) dissociation of TiCl3 to TiCl2 at 450° C. in vacuum followed by removal of gaseous titanium tetrachloride from the reaction zone, condensation to the liquid, and returning back into the reaction retort, (d) dissociation of TiCl2 in vacuum at 750-850° C. to manufacture fine powder of metallic titanium and titanium tetrachloride, whereby hydrogen heated up to 1000° C. is used to accelerate this reaction, and (e) saturation of the fine titanium powder by hydrogen at 400-640° C. to manufacture final product of titanium hydride powder which is free of oxygen or nitrogen. The semi-continuous process includes the Kroll's process as the very first step.
Owner:ADMA PRODS

Integrated milling equipment for welding groove of large irregular medium plate structure

The invention discloses integrated milling equipment for a welding groove of a large irregular medium plate structure. The integrated milling equipment comprises a milling cutter system component, a fixed-depth profile modeling component, a milling cutter adjusting component, a normal-direction support component, a horizontal tracking component, a milling cutter box floating component, a 90-degree reversing component, a height raising component, a groove length displacement component and a milling cutter box body. Firstly, separated weldments are assembled into an integrated weldment; afterwards, the welding groove is integrally machined; finally, welding is performed; in this way, the machining productivity of the welding groove is increased to at least double. With regard to integrated machining of the welding groove, the welding groove is machined through one milling cutter at a time, and therefore the consistency and reliability of the size of welding seams of the welding groove integrally machined are higher; the integrated milling equipment is quite beneficial to assembly quality guarantee of the weldments and the dimensional accuracy of the welded product; the machining cost of the welding groove is lower; the dimensional consistency of the welding groove is quite high, and single-sided weld with double-sided formation can usually be achieved; in this way, the welding productivity is further increased, and the production cycle is further shortened.
Owner:武汉纳瑞格智能设备有限公司

Method for recycling rubber-containing wastes

The inventive method includes thermal liquefaction of wastes in an organic solvent at a temperature above 270° C. and a pressure up to 6 MPa. The liquid fraction is separated from the undissolved product. The liquid fraction is distilled into the fraction with the boiling temperature below 220° C. and the fraction with the boiling temperature above 220° C. Alkyl benzene or the gasoline fraction with a boiling temperature below 220° C. is used as an organic solvent at the start-up of the process. Thermal liquefaction of a batch of wastes is carried out in an organic solvent at a temperature from 280° C. to 435° C. and a pressure at least 2.9 MPa, the organic solvent-waste weight ratio being more than 1.0. The liquid fraction with the boiling temperature below 220° C. is subjected to catalytic reforming. A part of the liquid fraction, as subjected to catalytic reforming, with the boiling temperature below 220° C. is used as the target product, and the remaining part of the liquid fraction, as subjected to catalytic reforming, with the boiling temperature below 220° C. is used as a solvent and returned for thermal liquefaction of a new batch of wastes at a temperature from 280° C. to 435° C. and a pressure at least 2.9 MPa, the solvent-waste weight ratio being more than 1.0. The process of thermal liquefaction is continued in the said conditions of thermal liquefaction and catalytic reforming for the next and subsequent batches of wastes, while a part of the liquid fraction, as subjected to catalytic reforming, with the boiling temperature below 220° C. being returned for thermal liquefaction.
Owner:OBSCHESTVO S OGRANICHENNOY OTVETSTVENNOSTYU N T D TAMANNO
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