248results about "Silicon halogen compounds" patented technology

The invention relates to potassium feldspar decomposition and comprehensive utilization technology and in particular relates to a process for decomposing potassium feldspar by adopting a low-temperature semidry method for comprehensive utilization. The process comprises the steps of fully mixing potassium feldspar, fluorite and sulfuric acid, then adding the mixture to a converter reactor to react at 180-250 DEG C, separating SiF4 and HF generated through a reaction from a system under the condition of negative pressure, carrying out absorption with ethanol and water solution to prepare white carbon black, recovering fluorine resources in the process from the solution in the forms of ammonium fluoride and other aids by adopting the method of adding ammonia water and applying the recovered fluorine sources to decomposition of potassium feldspar and carrying out a series of processes such as extraction on the solids after a reaction to obtain calcium sulfate whisker, potassium fluosilicate, aluminium hydroxide and ferric sulfate products. Compared with the method for decomposing potassium feldspar by a high temperature method, the process has the advantages that the reaction conditions are mild and the requirements for equipment are lower; the white carbon black is directly prepared through gas hydrolysis, thus avoiding the tedious course from solid phase separation; and the fluorine resources introduced to the decomposition course are recycled by adopting the mode of ammonium fluoride, thus avoiding waste of the fluorine resources.

There is described an apparatus, a tubular laminar flow, plug flow reactor, for making silylamines and particularly trisilylamine (TSA) in high yields from ammonia gas and a monohalosilane gas. The apparatus can be a tubular flow reactor comprising a first portion of the reactor defining a gas entry zone, a second portion of the reactor defining a reaction zone and a third portion of the reactor defining a separation zone, the reaction zone providing a reactant contacting region. Trisilylamine can be recovered in the separation zone in a cold trap collection vessel.

Compositions and methods are disclosed which facilitate purification of oligomers and other compounds. The disclosed compositions are silyl compositions that can be directly coupled, or coupled through a linking group, to a compound of interest, preferably to an oligomer at the end of oligomer synthesis. The silicon atom includes between one and three sidechains that function as capture tags. In one embodiment, the capture tags are lipophilic, which allows a derivatized oligomer to be separated from failure sequences by reverse phase chromatography. In another embodiment, the capture tags are compounds with a known affinity for other compounds, which other compounds are preferably associated with a solid support to allow chromatographic separation. Examples include haptens, antibodies, and ligands. Biotin, which can bind to or interact with a streptavidin-bound solid support, is a preferred capture tag of this type.

This invention discloses a method for separating phosphorus and fluorine of kiln process phosphoric acid by absorption. The method comprises: sending relatively high temperature phosphoric acid after hydration in primary and secondary hydration columns to a circulation tank for cooling, pumping into the hydration columns for circulation, sending gases after primary and secondary absorption to a Venturi absorber for re-absorption, collecting the residual acid mist by a collector, sending the absorbed gas and tail gas after fluorine absorption together to a chemical absorption column, and exhausting the tail gas. Besides, qualified fluosilicic acid can be obtained from the fluorine-containing diluted H3PO4 in the collector. The method utilizes the air with residual heat in the kiln, and has such advantages as no extra energy consumption, high phosphorus and fluorine separation efficiency, high concentration and low fluorine content in obtained H3PO4, and low P2O5 content in obtained fluosilicic acid. The obtained fluosilicic acid has a wide concentration range and a high purity, and is easy to utilize.

Crystalline scintillator materials comprising nano-scale particles of metal halides are provided. The nano-scale particles are less than 100 nm in size. Methods are provided for preparing the particles. In these methods, ionic liquids are used in place of water to allow precipitation of the final product. In one method, the metal precursors and halide salts are dissolved in separate ionic liquids to form solutions, which are then combined to form the nano-crystalline end product. In the other methods, micro-emulsions are formed using ionic liquids to control particle size.

The phosphoric acid can be circularly heated and concentrated in a circulating loop formed from flash chamber, graphitic heat exchanger and axial-flow circulating pump, the diluted phosphoric acid can be added into the circulating loop from outlet pipe of graphitic heat exchanger, and the evaporated steam can be passed through the entrainment eliminator to remove entrained acid foam, then the steam is more passed through two-stage fluorine absorbing tower, sprayed and washed so as to recover fluoride in the gas phase. The vacuum required for flash chamber is provided by atmosphere condenser. Said invention can make wet phosphoric acid be concentrated to 48-50% P2O5 from 20-25% P2O5.

The invention relates to a separation device which adopts the pressurized continuous high-precision distillation for extracting trichlorosilane and method thereof, including a low-boiling-point compound separation tower, a high-boiling-point compound separation tower and a hydrogen or argon pressurizing system, wherein, the feeding materials enter the middle part of the low-boiling-point compound separation tower after passing by a raw material pre-heating heat exchanger, the low-boiling-point products are separated at the tower top of the low-boiling-point compound separation tower, and a trichlorosilane forerunning product discharge pipe line at the tower bottom is connected to enter the middle part of the high-boiling-point compound separation tower. The high-purity trichlorosilane product is obtained at the tower top. The purity of the purified trichlorosilane product by the process reaches more than 99.999 percent, wherein, the content of boron, phosphorous, iron and other impurities is all less than 10ppb, the content of the impurities of the mixture of the trichlorosilane and other low-boiling-point compounds and high-boiling-point compounds is less than 5.0ppm, the recovery rate of the process is larger than 98.0 percent, meanwhile, the pressurized continuous high-precision thermal coupling distillation and separation technology of the entire invention has simple process flow and lower energy consumption.

An inorganic polysilazane resin of the present invention has a Si/N ratio (i.e. a ratio of contained silicon atoms to contained nitrogen atoms) of 1.30 or more. The inorganic polysilazane resin having such a high Si content can be produced by, for example, a method in which an inorganic polysilazane compound containing both Si—NH and Si—Cl is heated to react NH with Cl, a method in which a silazane oligomer (polymer) that leaves no Si—Cl bond is synthesized and a dihalosilane is added to the synthesized silazane oligomer (polymer) to perform a thermal reaction, and the like. A siliceous film can be formed by, for example, applying a coating composition containing the inorganic polysilazane resin onto a base plate and then dried and the dried product is then oxidized by bringing the dried product into contact with water vapor or hydrogen peroxide vapor and water vapor under heated conditions.

A method for the production of inorganic aluminum substances and amorphous silica from aluminum oxide containing ores, comprising: (a) leaching of said ores with fluorosilicic acid to obtain aluminum fluosilicate solution; (b) filtering said leached solution from insoluble materials; and (c) washing said insoluble materials.

The invention relates to a method for recycling waste residue in manganese industry production. The method comprises the specific following steps: (1) pre-processing filter residue; (2) adding acid and leaching; (3) carrying out filtering and solid-liquid separation on ore slurry; (4) recovering hematite powder; (5) recovering manganese carbonate concentrate; and (6) preparing a nitrogen-phosphorus compound fertilizer base material. By the method, hematite powder, manganese carbonate concentrate and the nitrogen-phosphorus compound fertilizer base material can be recovered from leached press-filtered residue, the process is simple and is easy to achieve industrialization and meanwhile, the content of the heavy metal ingredients is in completely in conformity with national associated standards, treated wastewater and waste residue are free of harmful ingredients such as heavy metals, the environmental pressure is alleviated and the method has great promotional values.

A method and apparatus for refining silicon which can remove impurity elements such as phosphorus and antimony as well as impurity elements such as boron and carbon using an electron beam in the same vacuum chamber are provided. Silicon is irradiated and melted with an electron beam in a low vacuum inside a vacuum vessel, a compound-forming substance such as H₂O which reacts with boron or the like in the molten silicon and forms a vaporizable oxide is introduced into the vacuum chamber, and impurity elements such as boron having a low vapor pressure in a vacuum are evaporated from the molten silicon as part of the vaporizable compound. Silicon in the vacuum vessel is then irradiated with an electron beam in a high vacuum in the vacuum vessel, and impurity elements contained in the silicon having a high vapor pressure in a vacuum such as phosphorus are removed.

When high purity silicon is produced through a gas-phase reaction between silicon tetra-chloride and zinc in a reaction furnace, the produce silicon is obtained as block or molten state. after the reaction in which the silicon is not in contact with air and reaction temperature is maintained at melting point of the silicon or less.

The invention provides a process for forming a low k fluorine and carbon-containing silicon oxide dielectric material by reacting with an oxidizing agent one or more silanes that include one or more organofluoro silanes selected from: (a) an organofluoro silane containing two silicon atoms linked by one oxygen atom; (b) an organofluoro silane containing two silicon atoms linked by one or more carbon atoms, where the one or more carbon atoms each are bonded to one or more fluorine atoms, or to one or more organofluoro moieties, or to a combination thereof; and (c) an organofluoro silane containing a silicon atom bonded to an oxygen atom. The invention also provides a process for forming a low k fluorine and carbon-containing silicon oxide dielectric material by reacting with an oxidizing agent one or more silanes that include one or more organofluoro silanes characterized by the presence of Si—O bonds.

The invention relates to a treatment method for multi-crystalline silicon texturization etching waste liquid. The treatment method comprises the following steps: (a) under the stirring condition, adding an alkali metal compound in the waste liquid for reaction till precipitates are not generated any more, and filtering to obtain a first precipitate and first filtrate; (b) under the stirring condition, adding an alkaline earth metal compound in the first filtrate for reaction till precipitates are not generated, and filtering to obtain a second precipitate and second filtrate; (c) conducting condensation crystallization on the second filtrate to obtain a nitrate solid. The treatment method has the advantages that the alkali metal compound is added in the waste liquid for reaction till the precipitates are not generated any more, filtering is conducted, the alkaline earth metal compound is added in the another filtrate, filtering is conducted again, and finally, concentration is conducted, so that fluosilicic acid radical ions and fluorinions in the waste liquid can be removed, a fluosilicate solid, a fluoride salt solid and the nitrate solid can be obtained, and not only can the environment be protected, but also new economic benefits can be generated.

In the apparatus for producing trichlorosilane in which metal silicon powder supplied into the reactor is reacted with hydrogen chloride gas while being fluidized by the gas, thereby taking out trichlorosilane generated by the reaction from the upper part of the reactor, and a plurality of gas flow controlling members are installed at the internal space of the reactor along the vertical direction.

An industrial fluosilicic acid purification and white carbon black co-production method belongs to the technical field of inorganic acid chemical production and purification. The method comprises the following steps: contacting an industrial fluosilicic acid solution with silica powders and carrying out heating, and collecting silicon tetrafluoride gas obtained after heating; absorbing the obtained silicon tetrafluoride gas directly by absorption liquid, and carrying out hydrolysis reaction to obtain a mixture of a fluosilicic acid solution and hydrated silicon dioxide solid; and separating the mixture to obtain the fluosilicic acid solution and the hydrated silicon dioxide solid. The method does not waste fluorine atoms in the purification process, and thus application range and additional value of the industrial fluosilicic acid are improved.

The present invention provides a way to obtain SiCl4 with high activity and selectivity by allowing metal Si or a chlorosilane having HSi bond in the molecule to react with HCl in the coexistence of a specific metal and a specific single substance of an element. Metal Si or a chlorosilane having HSi bond in the molecule and HCl are react with each other in the coexistence of one or more metals of group VIII elements in periodic table and one or more single substances of group VB elements of the 3rd and succeeding period.

The present invention relates to a method for pretreating biomass instead of sodium hydroxide, fulfuric acid and vapor explosion. Said invention is characterized by that it adopts the following steps: pulverizing cellulose-live biomasses of crop straw and stalk, grass and wood, etc., removing impurity, making acid hydrolysis, separating and extracting cellulose, using cellulose to hydrolyze cellulose, using saccharomycetes to make fermentation to produce ethyl alcohol and recover silicon fluoride. The above-mentioned acid is hydrofluoric acid.

The invention discloses a separating method of aminolysis and hydrofluosilicic element of silicofluoride, which comprises the following steps: 1. adding solid ammonium fluosilicate or silicon tetrafluoride gas in the saturated ammonium fluoride circulating reacting liquid; putting raw material amino to proceed aminolysis reaction; 2. reducing slurry temperature; screening the reacted slurry; 3. filtering the screened silica suspension and ammonium fluoride crystal slurry to obtain saturated ammonium fluoride solution, silica solid and ammonium fluoride crystal; returning to former procedures as the circulating reacting liquid; washing the ammonium fluoride crystal; drying through normal drying method to obtain high-purity product. The invention can improves technological and economical index, which is fit for wet-producing phosphoric acid, phosphate fertilizer and other phosphor businesses.

The invention relates to a resource comprehensive utilization method for recovering fluorine from wet-process phosphoric acid. The method comprises the following steps of: absorbing SiF4 and HF gases generated in the wet-process phosphoric acid by using water, and preparing the gases into a hydrofluosilicic acid solution of which the mass percent concentration is 10-35%; mixing one of four solids including solid sodium sulfate, solid potassium sulfate, solid sodium chloride and solid potassium chloride with the hydrofluosilicic acid solution, and reacting for 0.1-2 hours at 30-80 DEG C under stirring to obtain a mixture; centrifugally separating the obtained mixture to obtain a solid and a filtrate; and washing the solid with water, and drying for 1-3 hours at 100-120 DEG C to obtain a sodium fluorosilicate or potassium fluorosilicate crystal. According to the method, a byproduct hydrofluosilicic acid in the wet-process phosphoric acid and sodium (potassium) sulfates or chlorides which are abundant and easily-available are used as raw materials, so that the cost is low, two products including sodium fluorosilicate and potassium fluorosilicate can be produced at the same time by using one set of equipment, and the maximum utilization ratio of the hydrofluosilicic acid can reach over 99%.