CN104018009B - Separating and purifying technology for bismuth metal - Google Patents

Separating and purifying technology for bismuth metal Download PDF

Info

Publication number
CN104018009B
CN104018009B CN201410275099.6A CN201410275099A CN104018009B CN 104018009 B CN104018009 B CN 104018009B CN 201410275099 A CN201410275099 A CN 201410275099A CN 104018009 B CN104018009 B CN 104018009B
Authority
CN
China
Prior art keywords
bismuth
molten metal
furnace
separating
distillation
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.)
Active
Application number
CN201410275099.6A
Other languages
Chinese (zh)
Other versions
CN104018009A (en
Inventor
吴声良
曹晓星
商亚军
林锡庭
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.)
Hunan Huaxin rare expensive Polytron Technologies Inc
Original Assignee
HUNAN HUAXIN NONERROUS METALS CO Ltd
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 HUNAN HUAXIN NONERROUS METALS CO Ltd filed Critical HUNAN HUAXIN NONERROUS METALS CO Ltd
Priority to CN201410275099.6A priority Critical patent/CN104018009B/en
Publication of CN104018009A publication Critical patent/CN104018009A/en
Application granted granted Critical
Publication of CN104018009B publication Critical patent/CN104018009B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • Y02W30/54

Abstract

The invention relates to a separating and purifying technology for bismuth metal, and belongs to the technical field of physical separation. The separating and purifying technology is specifically as follows: heating lead and bismuth alloy materials to 500-550 DEG C in an electric-arc furnace, so that the alloy materials are molten into molten metal; slowly pre-heating a distillation furnace while vacuum-pumping, and sucking the molten metal in an electric-arc furnace melting tank into a distillation plate of the distillation furnace by a guide tube; boiling and evaporating the molten metal in the distillation plate to produce bismuth steam; guiding the bismuth steam into a condensing cover for condensing and gathering, and collecting bismuth powder with purity not less than 99.5%; discharging and casting the un-evaporated molten metal as a lead ingot. The separating and purifying technology disclosed by the invention is less in equipment and investment, low in cost, low in energy consumption, small in environmental pollution, and almost free of waste gas, and does not produce wastewater, and is extremely few in waste residues.

Description

The separating and purifying method of bismuth metal
Technical field
The present invention relates to the separating and purifying method from a kind of bismuth metal, belong to Physical Separation Technology field.
Background technology
Bismuth, ordination number 83, silvery white or blush, have metalluster.The production technology comparative maturity of external bismuth metal, bismuth compounds kind is more, and Application Areas is comparatively wide, and use value is higher.Wherein bismuth metal main production process has three kinds: Bettertan-Kroll method, thermal process and electrolytic purification technology.Current domestic lead, bismuth isolation technique are mainly based on chlorination process and electrolytic process.But two kinds of methods all need to use chemical agent, and easy contaminate environment, environment toxic is large.
Summary of the invention
In order to solve environmental problem, the present invention proposes a kind of separating and purifying method of bismuth metal, this technology be simple, can continuous seepage and good reliability.Bismuth purity >=99.5% after separating-purifying.
Technical solution of the present invention is: a kind of separating and purifying method of bismuth metal, uses lead, bismuth alloy material, lead, bismuth alloy material is heated to 500-550 DEG C in electric arc furnace, makes it to be fused into molten metal, is stored in electric arc furnace molten bath; Preheating limit, slow for distilling furnace limit is vacuumized, as distilling furnace vacuum tightness≤20Pa, when preheating temperature is 800-1000 DEG C, by conduit, the molten metal in electric arc furnace molten bath is sucked in the distillation tray of distilling furnace; Continue to vacuumize; When vacuum tightness is lower than 10Pa, close distilling furnace pre-heating system, start to be heated to separately 1500 DEG C to distillation tray, and steady temperature is 1500 ± 2 DEG C, molten metal is seethed with excitement in distillation tray and evaporates to produce bismuth steam, bismuth steam is imported condensing cover condensation assemble, collect the bismuth meal of purity >=99.5%; Do not have the molten metal evaporated then to discharge and be cast into lead pig.
In above-mentioned leaded, bismuth alloy material, calculate by weight percentage, Fe, Cu, As, Cd are below 0.45%, and Sb is below 0.6%, and Ag is within 1.85%.
Beneficial effect of the present invention is: relative usage chemical agent or electrolytic process extract bismuth, and this technique (1) equipment and input are less, with low cost; (2) energy consumption is low, and environmental pollution is little, does not almost have waste gas, does not produce waste water, and waste residue is few; (3) isolated bismuth purity high (>=99.5%), without the need to follow-up continuation processing.
Embodiment
Below in conjunction with specific embodiment, the invention will be further described.
Leaded, bismuth alloy material 100g that the present embodiment adopts, calculate, Fe0.27%, Cu0.16%, As0.042%, Cd0.055%, Sb 0.46%, Ag 1.82% by weight percentage.
Lead, bismuth alloy material are heated to 500 DEG C in electric arc furnace, make it to be fused into molten metal, be stored in electric arc furnace molten bath; Preheating limit, slow for distilling furnace limit is vacuumized, as distilling furnace vacuum tightness 18Pa, when preheating temperature is 900 DEG C, by conduit, the molten metal in electric arc furnace molten bath is sucked in the distillation tray of distilling furnace; Continue to vacuumize; When vacuum tightness is lower than 9Pa, close distilling furnace pre-heating system, start to be heated to separately 1500 DEG C to distillation tray, and steady temperature is 1500 ± 2 DEG C, molten metal is seethed with excitement in distillation tray and evaporates to produce bismuth steam, bismuth steam is imported condensing cover condensation assemble, collect the bismuth meal 22g of purity >=99.5%; Do not have the molten metal evaporated then to discharge and be cast into lead pig 86g.

Claims (1)

1. a separating and purifying method for bismuth metal, uses lead, bismuth alloy material; It is characterized in that lead, bismuth alloy material to be heated to 500-550 DEG C in electric arc furnace, make it to be fused into molten metal, be stored in electric arc furnace molten bath; Preheating limit, slow for distilling furnace limit is vacuumized, as distilling furnace vacuum tightness≤20Pa, when preheating temperature is 800-1000 DEG C, by conduit, the molten metal in electric arc furnace molten bath is sucked in the distillation tray of distilling furnace; Continue to vacuumize; When vacuum tightness is lower than 10Pa, close distilling furnace pre-heating system, start to be heated to separately 1500 DEG C to distillation tray, and steady temperature is 1500 ± 2 DEG C, molten metal is seethed with excitement in distillation tray and evaporates to produce bismuth steam, bismuth steam is imported condensing cover condensation assemble, collect the bismuth meal of purity >=99.5%; Do not have the molten metal evaporated then to discharge and be cast into lead pig;
In above-mentioned leaded, bismuth alloy material, calculate by weight percentage, Fe, Cu, As, Cd are below 0.45%, and Sb is below 0.6%, and Ag is within 1.85%.
CN201410275099.6A 2014-06-19 2014-06-19 Separating and purifying technology for bismuth metal Active CN104018009B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410275099.6A CN104018009B (en) 2014-06-19 2014-06-19 Separating and purifying technology for bismuth metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410275099.6A CN104018009B (en) 2014-06-19 2014-06-19 Separating and purifying technology for bismuth metal

Publications (2)

Publication Number Publication Date
CN104018009A CN104018009A (en) 2014-09-03
CN104018009B true CN104018009B (en) 2015-05-27

Family

ID=51435001

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410275099.6A Active CN104018009B (en) 2014-06-19 2014-06-19 Separating and purifying technology for bismuth metal

Country Status (1)

Country Link
CN (1) CN104018009B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105779790A (en) * 2016-04-12 2016-07-20 永兴佳盛有色金属再生利用有限责任公司 Method for removing lead and purifying bismuth from lead-bismuth material through vacuum distillation
CN106048243B (en) * 2016-08-11 2018-06-05 永兴佳盛环保科技有限责任公司 A kind of method that high bismuth crude tin alloy vacuum distillation depth removes bismuth
CN108160305B (en) * 2018-02-08 2019-10-18 韶关学院 A kind of mixed metal powder separation method and atmosphere furnace used

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10158754A (en) * 1996-11-26 1998-06-16 Dowa Mining Co Ltd Production of high-purity bismuth and apparatus for production
CN101525694A (en) * 2009-04-17 2009-09-09 深圳市中金岭南有色金属股份有限公司韶关冶炼厂 Separation process for material containing lead, antimony, copper, bismuth and silver
CN101696469A (en) * 2009-10-29 2010-04-21 昆明理工大学 Method for separating multi-element alloy of lead, bismuth, gold, silver and copper
CN102168179A (en) * 2011-04-07 2011-08-31 赵志强 Technology for producing Au and Ag from precious Pb by vacuum distillation

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10158754A (en) * 1996-11-26 1998-06-16 Dowa Mining Co Ltd Production of high-purity bismuth and apparatus for production
CN101525694A (en) * 2009-04-17 2009-09-09 深圳市中金岭南有色金属股份有限公司韶关冶炼厂 Separation process for material containing lead, antimony, copper, bismuth and silver
CN101696469A (en) * 2009-10-29 2010-04-21 昆明理工大学 Method for separating multi-element alloy of lead, bismuth, gold, silver and copper
CN102168179A (en) * 2011-04-07 2011-08-31 赵志强 Technology for producing Au and Ag from precious Pb by vacuum distillation

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
陈枫.铋铅合金真空蒸馏脱铅规律研究.《有色金属(冶炼部分)》.1992,(第1期), *

Also Published As

Publication number Publication date
CN104018009A (en) 2014-09-03

Similar Documents

Publication Publication Date Title
CN101560606B (en) Deleading method through vacuum distillation of noble lead materials
CN105969989B (en) High impurity copper ANODE SLIME TREATMENT new process
CN107217145A (en) A kind of method that copper anode mud vacuum reduction takes off lead antimony bismuth selen-tellurjum arsenic
CN101570827B (en) Method for distilling and purifying crude tin alloy in vacuum
CN107287432B (en) A method of recycling zinc, copper, cadmium from the copper-cadmium slag of zinc hydrometallurgy
CN102492861B (en) Fire refining method of crude tin
CN102465209B (en) Method and vacuum distillation device for preparing high-purity neodymium
CN101892496B (en) Method for preparing high-purity 5N tellurium from 3N crude tellurium
CN104018009B (en) Separating and purifying technology for bismuth metal
CN100494430C (en) Method for producing zinc alloy from zinc dross
CN104032133A (en) Method for recovering metal indium and tin from ITO waste target
JP2024508599A (en) Separation and purification method of high antimony crude tin
CN104651627A (en) Method for separating antimony from tin-antimony alloy by vacuum distillation
CN109371244A (en) A method of be enriched with and open a way from zinc hydrometallurgy leachate using zinc powder purification slag impurity
KR20140037277A (en) Method for producing calcium of high purity
CN104109766B (en) Technology for separating and purifying bismuth from lead-bismuth alloy
CN105238935B (en) A kind of electroslag remelting slag system
CN204058569U (en) A kind of system of vacuum distilling separating-purifying bismuth
CN108411118A (en) Lead bismuth alloy is electrolysed vacuum distillation impurity removal process and its application of leading portion
CN101314823B (en) Method for extracting thallium from thallium containing slag
CN104018000A (en) Process for separating and treating noble lead materials in vacuum
CN105779790A (en) Method for removing lead and purifying bismuth from lead-bismuth material through vacuum distillation
CN106367609B (en) A kind of thick golden vacuum refining method of purification
CN104495853B (en) A kind of industrial silicon refining method
CN107245583B (en) Method for preparing zinc-copper alloy from copper-cadmium slag

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: Jiangbei Industrial Park 423400 Chenzhou city of Hunan province Zixing Economic Development Zone

Patentee after: Hunan Huaxin rare expensive Polytron Technologies Inc

Address before: Jiangbei Industrial Park 423400 Chenzhou city of Hunan Province in Zixing City Huaxin company

Patentee before: Hunan Huaxin Nonerrous Metals Co., Ltd.