CN104591300A - Method for preparing cobalt carbonyl - Google Patents

Method for preparing cobalt carbonyl Download PDF

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Publication number
CN104591300A
CN104591300A CN201410733238.5A CN201410733238A CN104591300A CN 104591300 A CN104591300 A CN 104591300A CN 201410733238 A CN201410733238 A CN 201410733238A CN 104591300 A CN104591300 A CN 104591300A
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CN
China
Prior art keywords
cobalt
carbonyl
granule
gas
synthesis reactor
Prior art date
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Pending
Application number
CN201410733238.5A
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Chinese (zh)
Inventor
杨志强
王芳镇
肖冬明
江龙
王良
王大窝
孙渊君
孙顺盈
朱纪念
李志鹏
谢玉琴
何云霞
李琛
廖永晖
杨超
魏小海
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Jinchuan Group Co Ltd
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Jinchuan Group Co Ltd
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Publication date
Application filed by Jinchuan Group Co Ltd filed Critical Jinchuan Group Co Ltd
Priority to CN201410733238.5A priority Critical patent/CN104591300A/en
Publication of CN104591300A publication Critical patent/CN104591300A/en
Pending legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention relates to a method for preparing cobalt carbonyl. The method is characterized by comprising employing a cobalt particle as a raw material, performing carbonylation on the cobalt particle with CO in a high-pressure synthesis kettle for generating a cobalt carbonyl gas, and condensating the cobalt carbonyl gas to form cobalt carbonyl. The method for preparing cobalt carbonyl is simple in technology and is suitable for large-scale production.

Description

A kind of method preparing cobalt-carbonyl
Technical field
The present invention relates to a kind of method preparing cobalt-carbonyl.
Background technology
Cobalt-carbonyl is a kind of important carbonylcomplex, is also a kind of important catalyzer.Common monokaryon cobalt-carbonyl mainly contains three kinds of form: Co 2(CO) 8, HCo (CO) 4and Na [Co (CO) 4].The catalyst activity made due to cobalt-carbonyl is high, and cost ratio Pt, Pd, Rh complex compound is cheap, therefore receives much concern.Its synthetic method is a difficult problem all the time, does not make substantial progress.
Summary of the invention
Object of the present invention develop a kind of technique simple, mass-producing can prepare the method for cobalt-carbonyl.
To achieve these goals, the present invention by the following technical solutions.
Prepare a method for cobalt-carbonyl, it is characterized in that its preparation process adopts cobalt granule to be raw material, cobalt granule and CO are carried out carbonylation at Autoclaves for synthesis and generates cobalt-carbonyl gas, then cobalt-carbonyl that cobalt-carbonyl gas cold is congealed into.
A kind of method preparing cobalt-carbonyl of the present invention, it is characterized in that its cobalt granule is cobalt powder or the shrend cobalt be made up of electrodeposited cobalt or levigate cobalt powder, its particle diameter is less than 5mm.
A kind of method preparing cobalt-carbonyl of the present invention, it is characterized in that cobalt granule is placed in Autoclaves for synthesis by preparation process, by passing into the high-purity CO being heated to 150-170 DEG C bottom synthesis reactor, control synthesis reactor pressure 20-25MPa, CO and cobalt granule carbonylation generate cobalt-carbonyl gas, and synthetic gas is discharged by synthesis reactor top, through interchanger, synthetic gas temperature are reduced to 20-25 DEG C, cobalt-carbonyl gas cold congeals into cobalt-carbonyl particle, is packaged into vial in after being collected by strainer.
A kind of method preparing cobalt-carbonyl of the present invention, employing cobalt granule is raw material, is reacted by cobalt granule, prepare cobalt-carbonyl in reactor Yu by the carbon monoxide gas of reactor, can realize suitability for industrialized production.
Embodiment
A kind of method preparing cobalt-carbonyl, its preparation process adopts cobalt powder or the shrend cobalt be made up of electrodeposited cobalt or levigate cobalt granule to be raw material, raw material particle size should be less than 5mm, cobalt granule is placed in Autoclaves for synthesis, by passing into the high-purity CO being heated to 150-170 DEG C bottom synthesis reactor, control synthesis reactor pressure 20-25MPa, CO and cobalt granule carbonylation generate cobalt-carbonyl gas, synthetic gas is discharged by synthesis reactor top, through interchanger, synthetic gas temperature is reduced to 20-25 DEG C, cobalt-carbonyl gas cold congeals into cobalt-carbonyl particle, be packaged in vial after being collected by strainer.
Embodiment 1
Get cobalt powder 2000g, be placed in Autoclaves for synthesis, by passing into the high-purity CO being heated to 150 DEG C bottom synthesis reactor, control synthesis reactor pressure 20MPa, CO and cobalt powder carbonylation generate cobalt-carbonyl gas, and synthetic gas is discharged by synthesis reactor top, through interchanger, synthetic gas temperature are reduced to 20-25 DEG C, cobalt-carbonyl gas cold congeals into cobalt-carbonyl particle, is packaged into vial after being collected by strainer.
Embodiment 2
Get cobalt granule 2000g; be placed in Autoclaves for synthesis; by passing into the high-purity CO being heated to 160 DEG C bottom synthesis reactor; control synthesis reactor pressure 22MPa; CO and cobalt granule are combined to and generate cobalt-carbonyl gas, and synthetic gas is discharged by synthesis reactor top, through interchanger, synthetic gas temperature is reduced to 20-25 DEG C; cobalt-carbonyl gas cold congeals into cobalt-carbonyl particle, is packaged into vial after being collected by strainer.
Embodiment 3
Get particle diameter and be less than the levigate cobalt granule 2000g of 5mm; be placed in Autoclaves for synthesis; by passing into the high-purity CO being heated to 170 DEG C bottom synthesis reactor; control synthesis reactor pressure 25MPa; CO and cobalt granule are combined to and generate cobalt-carbonyl gas, and synthetic gas is discharged by synthesis reactor top, through interchanger, synthetic gas temperature is reduced to 20-25 DEG C; cobalt-carbonyl gas cold congeals into cobalt-carbonyl particle, is packaged into vial after being collected by strainer.

Claims (3)

1. prepare a method for cobalt-carbonyl, it is characterized in that its preparation process adopts cobalt granule to be raw material, cobalt granule and CO are carried out carbonylation at Autoclaves for synthesis and generates cobalt-carbonyl gas, then cobalt-carbonyl that cobalt-carbonyl gas cold is congealed into.
2. a kind of method preparing cobalt-carbonyl according to claim 1, it is characterized in that its cobalt granule is cobalt powder or the shrend cobalt be made up of electrodeposited cobalt or levigate cobalt powder, its particle diameter is less than 5mm.
3. a kind of method preparing cobalt-carbonyl according to claim 1, it is characterized in that cobalt granule is placed in Autoclaves for synthesis by preparation process, by passing into the high-purity CO being heated to 150-170 DEG C bottom synthesis reactor, control synthesis reactor pressure 20-25MPa, CO and cobalt granule carbonylation generate cobalt-carbonyl gas, and synthetic gas is discharged by synthesis reactor top, through interchanger, synthetic gas temperature are reduced to 20-25 DEG C, cobalt-carbonyl gas cold congeals into cobalt-carbonyl particle, is packaged into vial in after being collected by strainer.
CN201410733238.5A 2014-12-07 2014-12-07 Method for preparing cobalt carbonyl Pending CN104591300A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410733238.5A CN104591300A (en) 2014-12-07 2014-12-07 Method for preparing cobalt carbonyl

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410733238.5A CN104591300A (en) 2014-12-07 2014-12-07 Method for preparing cobalt carbonyl

Publications (1)

Publication Number Publication Date
CN104591300A true CN104591300A (en) 2015-05-06

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Family Applications (1)

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CN201410733238.5A Pending CN104591300A (en) 2014-12-07 2014-12-07 Method for preparing cobalt carbonyl

Country Status (1)

Country Link
CN (1) CN104591300A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB298714A (en) * 1927-07-28 1928-10-18 Ig Farbenindustrie Ag Improvements in the manufacture and production of cobalt carbonyl
GB307112A (en) * 1927-12-03 1929-03-04 Ig Farbenindustrie Ag Improvements in the production of cobalt carbonyl
CN1821095A (en) * 2006-03-17 2006-08-23 金川集团有限公司 Process for producing carbonyl iron
CN102719801A (en) * 2012-06-05 2012-10-10 金川集团股份有限公司 Method for preparing nickel foil
CN103723777A (en) * 2013-12-12 2014-04-16 金川集团股份有限公司 Method for preparing carbonyl iron through medium pressure continuous gasification

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB298714A (en) * 1927-07-28 1928-10-18 Ig Farbenindustrie Ag Improvements in the manufacture and production of cobalt carbonyl
GB307112A (en) * 1927-12-03 1929-03-04 Ig Farbenindustrie Ag Improvements in the production of cobalt carbonyl
CN1821095A (en) * 2006-03-17 2006-08-23 金川集团有限公司 Process for producing carbonyl iron
CN102719801A (en) * 2012-06-05 2012-10-10 金川集团股份有限公司 Method for preparing nickel foil
CN103723777A (en) * 2013-12-12 2014-04-16 金川集团股份有限公司 Method for preparing carbonyl iron through medium pressure continuous gasification

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Application publication date: 20150506