CN111041237A - Chromium removal method in production and refining process of antimony smelting reverberatory furnace - Google Patents

Chromium removal method in production and refining process of antimony smelting reverberatory furnace Download PDF

Info

Publication number
CN111041237A
CN111041237A CN201911238881.XA CN201911238881A CN111041237A CN 111041237 A CN111041237 A CN 111041237A CN 201911238881 A CN201911238881 A CN 201911238881A CN 111041237 A CN111041237 A CN 111041237A
Authority
CN
China
Prior art keywords
chromium
antimony
refining
liquid
production
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.)
Withdrawn
Application number
CN201911238881.XA
Other languages
Chinese (zh)
Inventor
王卫国
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.)
Guangxi Wanshizhi Rare Precious Metal Technology Co Ltd
Original Assignee
Guangxi Wanshizhi Rare Precious Metal Technology 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 Guangxi Wanshizhi Rare Precious Metal Technology Co Ltd filed Critical Guangxi Wanshizhi Rare Precious Metal Technology Co Ltd
Priority to CN201911238881.XA priority Critical patent/CN111041237A/en
Publication of CN111041237A publication Critical patent/CN111041237A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B30/00Obtaining antimony, arsenic or bismuth
    • C22B30/02Obtaining antimony
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B9/00General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
    • C22B9/10General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention relates to the technical field of non-ferrous metal antimony smelting, and discloses a chromium removing method in the production and refining process of an antimony smelting reverberatory furnace, wherein an alkali metal compound is used as a chromium removing agent, the chromium content of antimony liquid before refining is 0.03-0.05%, the weight of the antimony liquid is 45-50 tons, 1.5-20 tons of prepared tin removing agent is added at 950-1000 ℃, slag is discharged after blowing and stirring for 1 hour, the chromium content of the antimony liquid is 0.0001-0.0006% in a sampling test, the chromium-removed slag produced after the reaction is completed can float on the surface of the antimony liquid, and the chromium-removed scum is discharged out of the furnace from an operation door. The technical scheme of the invention can effectively remove the impurity chromium element in the antimony, has obvious economic benefit and has important significance for expanding the application field of antimony products in industry.

Description

Chromium removal method in production and refining process of antimony smelting reverberatory furnace
Technical Field
The invention relates to the technical field of non-ferrous metal antimony smelting, in particular to a chromium removal method in the production and refining process of an antimony smelting reverberatory furnace.
Background
In the smelting process of non-ferrous metal antimony, impurity chromium influences the quality of antimony products and restricts the application of antimony products in industry, but an effective chromium removal method in the production and refining process of an antimony smelting reverberatory furnace is not available in the industry to date.
During the course of research and practice on this method, the inventors of the present invention found that: a compound comprising an alkali metal; the alkali metal compound is used alone or mixed with several kinds of alkali metal compounds in certain proportion to prepare the chromium eliminating agent for refining antimony, so that the chromium eliminating agent has excellent chromium eliminating effect in the refining process of the reverberatory furnace for smelting and producing antimony, has obvious economic benefit and has important significance in expanding the application field of antimony products in industry.
Disclosure of Invention
The invention aims to provide a chromium removal method in the production and refining process of an antimony smelting reverberatory furnace, so as to achieve the effects of improving the production efficiency, reducing the energy consumption and realizing clean production.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows:
a chromium removing method in the production and refining process of an antimony smelting reverberatory furnace uses an alkali metal compound as a chromium removing agent, the chromium content of antimony liquid before refining is 0.03-0.04%, the weight of the antimony liquid is 45-50 tons, 1.5-20 tons of prepared tin removing agent is added at 950-1000 ℃, slag is discharged after blowing and stirring for 1 hour, the chromium content of the antimony liquid is 0.0006-0.0001% after sampling and testing, chromium removing slag produced after reaction is floated on the surface of the antimony liquid, and the chromium removing scum is taken out of the furnace from an operation door.
Preferably, the weight of the antimony liquid is 45 tons, the chromium content of the antimony liquid before refining is 0.03 percent, and the tin content of the antimony liquid after sampling and testing after refining is 0.0006 percent.
Preferably, the weight of the antimony liquid is 50 tons, the chromium content of the antimony liquid before refining is 0.04 percent, and the chromium content of the antimony liquid after sampling and testing after refining is 0.001 percent.
The technical scheme of the invention can produce good chromium removal effect in the refining process of the reverberatory furnace for antimony smelting production, has obvious economic benefit and has important significance for expanding the application field of antimony products in industry.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Example 1
A18 square meter reverberatory furnace is used for refining chromium-removing operation, a certain alkali metal compound is used as a chromium-removing agent, 0.04 percent of antimony liquid contains chromium before refining, 50 tons of antimony liquid is estimated by weight, 1.5 tons of prepared chromium-removing agent is added at 950-1000 ℃, slag is discharged after blowing and stirring for 1 hour, a sample is taken for testing 0.001 percent of chromium in the antimony liquid, the chromium-removing effect is better than an expected value, and the chromium-removing effect is obvious.
Example 2
A16 square meter reverberatory furnace is used for refining chromium-removing operation, a certain alkali metal compound is used as a chromium-removing agent, 0.03 percent of antimony liquid contains chromium before refining, 45 tons of antimony liquid is estimated by weight, 1 ton of prepared chromium-removing agent is added at 950-1000 ℃, slag is discharged after 1 hour of blast stirring, 0.0006 percent of antimony liquid containing chromium is sampled and tested, the chromium-removing effect is superior to an expected value, and the chromium-removing effect is obvious.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.

Claims (3)

1. A chromium removing method in the production and refining process of an antimony smelting reverberatory furnace is characterized in that an alkali metal compound is used as a chromium removing agent, the chromium content of antimony liquid before refining is 0.03-0.04%, the weight of the antimony liquid is 45-50 tons, 1.5-20 tons of prepared tin removing agent is added at 950-1000 ℃, slag is discharged after blowing and stirring for 1 hour, the chromium content of the antimony liquid is 0.0006-0.0001% after sampling and testing, chromium removing slag produced after reaction is floated on the surface of the antimony liquid, and the chromium removing scum is removed out of the furnace from an operation door.
2. The method for removing chromium in the production and refining process of the antimony smelting reverberatory furnace according to claim 1, wherein the weight of the antimony liquid is 45 tons, the chromium content in the antimony liquid before refining is 0.03%, and the tin content in the antimony liquid after sampling and testing after refining is 0.0006%.
3. The method for removing chromium in the production and refining process of the antimony smelting reverberatory furnace according to claim 1, wherein the weight of the antimony liquid is 50 tons, the chromium content in the antimony liquid before refining is 0.04%, and the chromium content in the antimony liquid after sampling and testing after refining is 0.001%.
CN201911238881.XA 2019-12-06 2019-12-06 Chromium removal method in production and refining process of antimony smelting reverberatory furnace Withdrawn CN111041237A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201911238881.XA CN111041237A (en) 2019-12-06 2019-12-06 Chromium removal method in production and refining process of antimony smelting reverberatory furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201911238881.XA CN111041237A (en) 2019-12-06 2019-12-06 Chromium removal method in production and refining process of antimony smelting reverberatory furnace

Publications (1)

Publication Number Publication Date
CN111041237A true CN111041237A (en) 2020-04-21

Family

ID=70234780

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201911238881.XA Withdrawn CN111041237A (en) 2019-12-06 2019-12-06 Chromium removal method in production and refining process of antimony smelting reverberatory furnace

Country Status (1)

Country Link
CN (1) CN111041237A (en)

Similar Documents

Publication Publication Date Title
CN111041233A (en) Cadmium removing agent for antimony smelting production and application thereof
CN106566925A (en) Method for achieving acid mixing, curing and leaching of vanadium through stone coal vanadium ore
CN112708786A (en) Method for recycling scandium from aluminum-scandium alloy target material waste
CN103451673B (en) The production method of electrolytic metal Mn
CN111057872A (en) Bismuth removing method in refining process of antimony smelting reverberatory furnace
US1719168A (en) Pickling of metals, etc.
CN110684904A (en) Method for recovering copper and tin in waste tinned copper wire
CN111041237A (en) Chromium removal method in production and refining process of antimony smelting reverberatory furnace
CN104060093B (en) A kind for the treatment of process of waste water neutralize gypsum tailings
CN111041223A (en) Zinc removal method in production and refining process of antimony smelting reverberatory furnace
CN111057870A (en) Tin removing method in refining process of antimony smelting reverberatory furnace
CN113564384B (en) Production method of refined antimony with ultralow arsenic content
CN205295386U (en) Aluminium ash preparation deoxidier device
CN111057860A (en) Chromium removing agent for refining antimony smelting reverberatory furnace and application thereof
CN111020226A (en) Tin removing agent in refining process of antimony smelting reverberatory furnace and application thereof
CN111320455A (en) Method for preparing high-strength GRC extruded board from graphite tailings
CN111041236A (en) Zinc removal agent for refining antimony smelting reverberatory furnace and application thereof
CN102826582A (en) Method for producing impurity-containing liquid calcium chloride by using converter dedusting wastewater
CN112744821A (en) Quartz sand acid elution purification process
CN111041235A (en) Copper removal method in refining process of antimony smelting reverberatory furnace
CN111041231A (en) Copper removing agent for antimony smelting production and application thereof
CN111041238A (en) Tellurium removal agent for antimony smelting production and application thereof
CN111041232A (en) Iron remover for antimony smelting production and application thereof
CN103255304A (en) Interior purification technology for molten aluminum smelter
CN111057871A (en) Bismuth removing agent for antimony smelting production and application thereof

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
WW01 Invention patent application withdrawn after publication
WW01 Invention patent application withdrawn after publication

Application publication date: 20200421