CN112126800A - Pre-pumping method for assembling reactor and large cover in titanium sponge production - Google Patents
Pre-pumping method for assembling reactor and large cover in titanium sponge production Download PDFInfo
- Publication number
- CN112126800A CN112126800A CN202011082338.8A CN202011082338A CN112126800A CN 112126800 A CN112126800 A CN 112126800A CN 202011082338 A CN202011082338 A CN 202011082338A CN 112126800 A CN112126800 A CN 112126800A
- Authority
- CN
- China
- Prior art keywords
- reactor
- vacuum
- large cover
- end system
- mechanical pump
- 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
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B34/00—Obtaining refractory metals
- C22B34/10—Obtaining titanium, zirconium or hafnium
- C22B34/12—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
- C22B34/1263—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction
- C22B34/1268—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams
- C22B34/1272—Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams reduction of titanium halides, e.g. Kroll process
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B5/00—General methods of reducing to metals
- C22B5/02—Dry methods smelting of sulfides or formation of mattes
- C22B5/04—Dry methods smelting of sulfides or formation of mattes by aluminium, other metals or silicon
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
The pre-pumping method for assembling the reactor and the large cover in the production of the titanium sponge comprises the following steps: after the reactor and the large cover are assembled, connecting pipelines, closing a valve, opening a clamp, starting a mechanical pump, evacuating a cold end system formed by the reactor and the large cover, keeping the reading of a vacuum meter of the cold end system at-75 to-90 kilopascals, evacuating for 24 hours, then stopping the mechanical pump, detecting the leakage by using a Mach vacuum gauge, and detecting the leakage in the vacuum degree range of 0 to 3 pascals, wherein the leakage is qualified; and after the leakage detection is qualified, opening a valve, starting a mechanical pump, enabling hot air of the heat supply device to enter a cold end system assembled by the reactor and the large cover through a conveying pipe, keeping the reading of a vacuum meter of the cold end system at-75 to-90 kPa, heating for 6 hours to remove moisture, then closing the valve, simultaneously cutting off a vacuum hose pipeline through a clamp, and stopping the mechanical pump to finish the pre-pumping work. The invention can completely remove the water of chloride and low-price substances, the early stage vacuum degree of the distillation stage is not influenced, and the vacuum system is not polluted, so that the product quality is ensured.
Description
Technical Field
The invention relates to a pre-pumping method for assembling a reactor and a large cover in the production of titanium sponge.
Background
At present, large-scale titanium sponge production at home and abroad adopts a magnesium method to produce titanium sponge, a furnace type adopts a combination method, namely a hot end system and a cold end system, wherein the hot end system and the cold end system are formed by assembling a reactor and a large cover, when in reduction, fine titanium tetrachloride is added into the hot end system at a high temperature state to react with liquid fine magnesium contained in the reactor to prepare metal titanium and magnesium chloride, then the cold end system is connected beside the hot end system through a passage according to the physical characteristics of various components of distillate, low-price titanium, magnesium chloride and magnesium in the reactor of the hot end system are distilled into the reactor of the cold end system at a high temperature and a high vacuum state, the pure titanium sponge is obtained by the hot end system, and the low-price titanium, magnesium chloride and magnesium are collected in the reactor of the cold end system. After distillation is finished, the cold end system is hung into the heating furnace to become a new hot end system. In the titanium sponge production, reactor and big lid belong to important equipment, after the titanium sponge reduction, before carrying out the distillation, preparation process must clear up, assemble into cold junction system, work such as sampling leak in advance to the attachment on reactor and big lid surface, just gets into distillation system's cold junction. The method is recycled until the reactor or the large cover is scrapped, but the reactor and the large cover are used repeatedly, a large amount of low-valent substances and chlorides remained in production are adsorbed frequently, the chlorides and the low-valent substances have strong water absorption and are easy to hydrolyze, and a large amount of chlorides and low-valent substances cannot be removed thoroughly in the cleaning process of the preparation process, so that the vacuum degree at the early stage of the distillation stage is influenced and a vacuum system is polluted along with the investment of the reactor and the large cover in production after the chlorides and the low-valent substances are hydrolyzed; residual low-valent substances and chlorides affect the quality of products after absorbing water.
Disclosure of Invention
The invention aims to solve the problems that in the prior art, a great amount of chlorides and low-price substances cannot be thoroughly removed during cleaning in a preparation process, so that the early vacuum degree of a distillation stage is influenced and a vacuum system is polluted along with the investment of a reactor and a large cover in production after the chlorides and the low-price substances are hydrolyzed; but also the residual low-price substances and chlorides affect the quality of the product after absorbing water.
The technical scheme of the invention is as follows:
the pre-pumping method for assembling the reactor and the large cover in the production of the titanium sponge comprises a pre-pumping device, wherein the pre-pumping device consists of a conveying pipe 1, a valve 2, a magnesium chloride pipe 3, a reactor 4, a large cover 5, a clamp 6, a vacuum hose 7, a pumping pipe 8, a mechanical pump 9 and a heat supply device 10;
the method comprises the following steps: after the reactor 4 and the large cover 5 are assembled, connecting pipelines, closing the valve 2, opening the clamp 6, starting the mechanical pump 9, evacuating a cold end system formed by the reactor 4 and the large cover 5 to ensure that the reading of a vacuum meter of the cold end system is kept at minus 75 to minus 90 kilopascals for 24 hours, then stopping the mechanical pump 9, detecting the leakage by using a Mach vacuum gauge, and ensuring that the vacuum degree of the Mach vacuum gauge is reduced within the range of 0 to 3 pascals to be qualified; and after the leakage detection is qualified, opening the valve 2, starting the mechanical pump 9, enabling hot air of the heat supply device 10 to enter a cold end system assembled by the reactor 4 and the large cover 5 through the conveying pipe 1, keeping the reading of a vacuum meter of the cold end system at-75 to-90 kPa, heating for 6 hours to remove moisture, then closing the valve 2, simultaneously cutting off a vacuum hose 7 pipeline through the clamp 6, and stopping the mechanical pump 9, thus finishing the pre-pumping work.
The invention has the following specific advantages and positive effects:
the invention can completely remove the water of chloride and low-price substances, the early stage vacuum degree of the distillation stage is not influenced, and the vacuum system is not polluted, so that the product quality is ensured.
Drawings
FIG. 1 is a schematic view of an apparatus used in the present invention.
In the figure: 1-conveying pipe, 2-valve, 3-magnesium chloride pipe, 4-reactor, 5-large cover, 6-clamp, 7-vacuum hose, 8-evacuation pipe, 9-mechanical pump and 10-heat supply device.
Detailed Description
The present invention will be described in further detail with reference to the drawings, but it should not be construed that the scope of the subject matter of the present invention is limited to the following embodiments, and various modifications, substitutions and alterations made based on the knowledge and conventional practices of the ordinary skill in the art are included in the scope of the present invention without departing from the technical spirit of the present invention.
As shown in figure 1, the pre-pumping method for assembling the reactor and the large cover in the production of the titanium sponge comprises a pre-pumping device, wherein the pre-pumping device consists of a conveying pipe 1, a valve 2, a magnesium chloride pipe 3, a reactor 4, a large cover 5, a clamp 6, a vacuum hose 7, an evacuation pipe 8, a mechanical pump 9 and a heat supply device 10;
the method comprises the following steps: after the reactor 4 and the large cover 5 are assembled, connecting pipelines, closing the valve 2, opening the clamp 6, starting the mechanical pump 9, evacuating a cold end system formed by the reactor 4 and the large cover 5 to ensure that the reading of a vacuum meter of the cold end system is kept at minus 75 to minus 90 kilopascals for 24 hours, then stopping the mechanical pump 9, detecting the leakage by using a Mach vacuum gauge, and ensuring that the vacuum degree of the Mach vacuum gauge is reduced within the range of 0 to 3 pascals to be qualified; and after the leakage detection is qualified, opening the valve 2, starting the mechanical pump 9, enabling hot air of the heat supply device 10 to enter a cold end system assembled by the reactor 4 and the large cover 5 through the conveying pipe 1, keeping the reading of a vacuum meter of the cold end system at-75 to-90 kPa, heating for 6 hours to remove moisture, then closing the valve 2, simultaneously cutting off a vacuum hose 7 pipeline through the clamp 6, and stopping the mechanical pump 9, thus finishing the pre-pumping work.
Claims (1)
1. The pre-pumping method for assembling the reactor and the large cover in the production of the titanium sponge comprises a pre-pumping device, wherein the pre-pumping device consists of a conveying pipe (1), a valve (2), a magnesium chloride pipe (3), a reactor (4), the large cover (5), a clamp (6), a vacuum hose (7), an evacuation pipe (8), a mechanical pump (9) and a heat supply device (10);
the method is characterized in that: the method comprises the following steps: after the reactor (4) and the large cover (5) are assembled, connecting pipelines, closing a valve (2), opening a clamp (6), starting a mechanical pump (9), evacuating a cold end system formed by the reactor (4) and the large cover (5), keeping the reading of a vacuum meter of the cold end system at-75 to-90 kilopascals, evacuating for 24 hours, then stopping the mechanical pump (9), detecting leakage by using a Mach vacuum gauge, and detecting the qualified leakage when the vacuum degree of the Mach vacuum gauge is reduced within the range of 0 to 3 pascals; and after the leakage detection is qualified, opening the valve (2), starting the mechanical pump (9), allowing hot air of the heat supply device (10) to enter a cold end system assembled by the reactor (4) and the large cover (5) through the conveying pipe (1), keeping the reading of a vacuum meter of the cold end system at-75 to-90 kPa, heating for 6 hours to remove moisture, then closing the valve (2), simultaneously cutting off a vacuum hose (7) pipeline through the clamp (6), and stopping the mechanical pump (9), thus completing the pre-pumping work.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011082338.8A CN112126800A (en) | 2020-10-12 | 2020-10-12 | Pre-pumping method for assembling reactor and large cover in titanium sponge production |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011082338.8A CN112126800A (en) | 2020-10-12 | 2020-10-12 | Pre-pumping method for assembling reactor and large cover in titanium sponge production |
Publications (1)
Publication Number | Publication Date |
---|---|
CN112126800A true CN112126800A (en) | 2020-12-25 |
Family
ID=73844106
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202011082338.8A Pending CN112126800A (en) | 2020-10-12 | 2020-10-12 | Pre-pumping method for assembling reactor and large cover in titanium sponge production |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN112126800A (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB768124A (en) * | 1953-06-13 | 1957-02-13 | Peter Spence & Sons Ltd | Improved method and apparatus for obtaining ductile titanium or zirconium |
CN1119266A (en) * | 1994-09-22 | 1996-03-27 | 范毅 | Water vapor separation technique and device in vacuum system |
CN101003861A (en) * | 2007-01-23 | 2007-07-25 | 遵义钛业股份有限公司 | Method and equipment for producing high-purified titanium |
CN101629248A (en) * | 2009-07-29 | 2010-01-20 | 遵义钛业股份有限公司 | Reduction distillation device for producing sponge titanium |
CN103925791A (en) * | 2014-04-16 | 2014-07-16 | 嵩县开拓者钼业有限公司 | Vacuum heating furnace |
CN107287449A (en) * | 2017-08-17 | 2017-10-24 | 东方弗瑞德(北京)科技有限公司 | A kind of argon gas introducing device and introducing method produced for magnesium method titanium sponge |
CN206609306U (en) * | 2017-03-23 | 2017-11-03 | 中国能源建设集团广东省电力设计研究院有限公司 | Vaccum-pumping equipment |
CN109854954A (en) * | 2019-04-16 | 2019-06-07 | 遵义钛业股份有限公司 | A kind of magnesium chloride caused during sponge titanium production automatic-discharging, waste gas collection device and production technology |
-
2020
- 2020-10-12 CN CN202011082338.8A patent/CN112126800A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB768124A (en) * | 1953-06-13 | 1957-02-13 | Peter Spence & Sons Ltd | Improved method and apparatus for obtaining ductile titanium or zirconium |
CN1119266A (en) * | 1994-09-22 | 1996-03-27 | 范毅 | Water vapor separation technique and device in vacuum system |
CN101003861A (en) * | 2007-01-23 | 2007-07-25 | 遵义钛业股份有限公司 | Method and equipment for producing high-purified titanium |
CN101629248A (en) * | 2009-07-29 | 2010-01-20 | 遵义钛业股份有限公司 | Reduction distillation device for producing sponge titanium |
CN103925791A (en) * | 2014-04-16 | 2014-07-16 | 嵩县开拓者钼业有限公司 | Vacuum heating furnace |
CN206609306U (en) * | 2017-03-23 | 2017-11-03 | 中国能源建设集团广东省电力设计研究院有限公司 | Vaccum-pumping equipment |
CN107287449A (en) * | 2017-08-17 | 2017-10-24 | 东方弗瑞德(北京)科技有限公司 | A kind of argon gas introducing device and introducing method produced for magnesium method titanium sponge |
CN109854954A (en) * | 2019-04-16 | 2019-06-07 | 遵义钛业股份有限公司 | A kind of magnesium chloride caused during sponge titanium production automatic-discharging, waste gas collection device and production technology |
Non-Patent Citations (5)
Title |
---|
《有色金属提取冶金手册》编辑委员会: "《有色金属提取冶金手册 稀有高熔点金属 上 W、Mo、Re、Ti》", 31 January 1999 * |
KEHUAN WANG等: ". Formability and microstructure evolution for hot gas forming of laser-welded TA15 titanium alloy tubes", 《MATERIALS & DESIGN》 * |
仵海东等: "《普通高等教育十三五规划教材 金属材料工程实验教程》", 31 July 2017 * |
董伟霞: "《陶瓷工艺基础》", 28 February 2017 * |
陈太武: "论镁法海绵钛生产中设备预处理的影响及改进", 《湖南有色金属》 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102259100B (en) | Method for cleaning electronic-grade polycrystalline silicon production device and process pipe | |
CN201737828U (en) | Device for cleaning attachments of tin bath and runner on float glass production line | |
CN103952776A (en) | Spinning component hydrolysis washing device and washing method thereof | |
CN212293714U (en) | Pre-pumping device for assembling reactor and large cover in titanium sponge production | |
CN112126800A (en) | Pre-pumping method for assembling reactor and large cover in titanium sponge production | |
CN201151738Y (en) | Reducing distillation reactor | |
CN102019661A (en) | Film making box | |
CN111961885A (en) | Pre-pumping device for assembling reactor and large cover in titanium sponge production | |
CN211527126U (en) | Novel phosphorus furnace tail gas comprehensive utilization system | |
CN204550789U (en) | Adopt graphite plate outside a kind of and clean stove | |
CN215905869U (en) | Purification device for coarse arsenic trioxide | |
CN216190940U (en) | Blanking pipeline for rubber plug machine | |
CN213558725U (en) | Automatic acid steaming cleaning device for integrated vertical overhead downward-pressing type hinge switch cover | |
CN112539990B (en) | Environment-friendly full-automatic electric heating high-temperature high-pressure digestion instrument combination device | |
CN206345881U (en) | A kind of device of high-pressure liquid or above-critical state quenching | |
CN207915993U (en) | A kind of energy saving die heater of bloom | |
CN208269636U (en) | A kind of vacuum cleaning oven that fiber process cleaning uses | |
CN203807604U (en) | Hydrolysis cleaning device of spinning component | |
CN2740590Y (en) | Apparatus for recovering and treating mud phosphorus | |
CN205710903U (en) | Gas turbine blade inner hole channel surface coating repair equipment | |
CN219160311U (en) | Temperature and pressure reducing device capable of effectively utilizing waste heat | |
CN209522896U (en) | A kind of stainless steel cure process device | |
CN207755786U (en) | A kind of concentrator based on condiment production | |
CN213599054U (en) | JN3018 type series metal Dewar flask | |
CN221608168U (en) | Electronic grade gas steel cylinder passivation system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20201225 |