CN1186249C - Prepn of copper-bearing synthetic gas purifier - Google Patents

Prepn of copper-bearing synthetic gas purifier Download PDF

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Publication number
CN1186249C
CN1186249C CN 01127263 CN01127263A CN1186249C CN 1186249 C CN1186249 C CN 1186249C CN 01127263 CN01127263 CN 01127263 CN 01127263 A CN01127263 A CN 01127263A CN 1186249 C CN1186249 C CN 1186249C
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China
Prior art keywords
preparation
levy
copper
synthetic gas
scavenging agent
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Expired - Fee Related
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CN 01127263
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Chinese (zh)
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CN1344672A (en
Inventor
袁亦然
毕智锋
李金鸿
石继全
陈文锋
朱伟
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Research Institute of Sinopec Nanjing Chemical Industry Co Ltd
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Research Institute of Nanjing Chemical Industry Group Co Ltd
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Priority to CN 01127263 priority Critical patent/CN1186249C/en
Publication of CN1344672A publication Critical patent/CN1344672A/en
Application granted granted Critical
Publication of CN1186249C publication Critical patent/CN1186249C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The present invention relates to a preparation method of a copper- based synthetic gas purifier, which belongs to the technical field of a catalyst. A Cu-Zn-Cr system is mainly adopted. A prepared purifier can effectively eliminate Fe (CO) 5 and Ni (CO) 4 in synthetic gas. Simultaneously, the prepared purifier can perform the function of eliminating S. The preparation method adopts the combination of a coprecipitation method and a mechanical mixing method. The purifier prepared by the method is suitable for the synthetic gas with CO, CO2 and H2, and is especially suitable for a carbinol synthesis device of the synthetic gas.

Description

The preparation method of copper-bearing synthetic gas purifier
Technical field: the invention belongs to catalyst technical field, be specifically related to a kind of preparation method of copper-bearing synthetic gas purifier.
Background technology: synthetic gas is the unstripped gas of a series of Cl chemical such as synthesizing methanol, dme, alkene, its building-up reactions catalyst system therefor often can make all to the more responsive a spot of impurity element of impurity element such as As, S, Cl, Fe, Ni etc. that the synthetic catalyst activity reduces greatly, by product increases, shorten catalyzer work-ing life, therefore, be necessary synthetic gas is purified, remove impurity elements such as As, S, Cl, Fe, Ni.The scavenging agent use that removes at present As, S, Cl element specially is more, and uses less at the scavenging agent of elements such as Fe, Ni.
Summary of the invention: the present invention is the preparation method that will propose a kind of copper-bearing synthetic gas purifier, adopts the Cu-Zn-Cr system.The scavenging agent of the present invention preparation can remove Fe, Ni in the synthetic gas effectively (in synthetic gas generally with Fe (CO) 5And Ni (CO) 4Form exists), also can play the effect of taking off S simultaneously.
The present invention adopts co-precipitation in conjunction with mechanical mixing, it mainly may further comprise the steps: concentration range is mixed at the soluble Zn salts solution that soluble copper salts solution and the concentration range of 10~250g/L is 10~250g/L, be the reaction of 5~20% precipitation agent with concentration then, the precipitation of making after filtration, oven dry is back and the compound mechanically mixing of chromium, through roasting, compression molding.
The scavenging agent of the present invention's preparation, copper zinc chrome ratio is Cu: Zn: Cr=1: (0.5~3): (0.5~3).
The used soluble copper salt of the present invention can be a nitrate; Soluble zinc salt can be a nitrate; Precipitation agent can be Na 2CO 3, also can be NaHCO 3The compound of chromium can be CrO 3
Be applicable to the scavenging agent of the inventive method preparation and contain CO, CO 2, H 2Synthetic gas, be particularly useful for synthetic gas synthesizing methanol device.
Embodiment: further specify content of the present invention below in conjunction with embodiment.
Embodiment 1:
Cu (the NO that 0.5L is contained 120g 3) 2Solution and 0.5L contain the Zn (NO of 115g 3) 2Solution mixes, and makes A solution, and be heated to 60~85 ℃ stand-by.With 180g NaHCO 3Be dissolved in the 3L deionized water, make B solution, and be heated to 65~85 ℃ stand-by.Under agitation B solution is poured into and carried out neutralization reaction in the A solution, controlled temperature is at 65~85 ℃ in the N-process, and control terminal point pH is 6.0~8.0, aging 20min, the slurries filtration that obtains thus, washing, in 90~120 ℃ the oven dry 6hr, the filter cake that obtains again with 50g CrO 3Mechanically mixing, granulation, in 250~400 ℃ of roasting 3hr, the material after the roasting is admixed 1~2% graphite, 5~15% water, is pressed into the tablet scavenging agent that gets product.
Embodiment 2: the Cu (NO that 0.5L is contained 120g 3) 2Solution and 0.5L contain the Zn (NO of 180g 3) 2Solution mixes, and makes A solution, and be heated to 60~85 ℃ stand-by.With 180g Na 2CO 3Be dissolved in the 3L deionized water, make B solution, and be heated to 65~85 ℃ stand-by.Under agitation B solution is poured into and carried out neutralization reaction in the A solution, controlled temperature is at 65~85 ℃ in the N-process, and control terminal point pH is 6.0~8.0, aging 20min, the slurries filtration that obtains thus, washing, in 90~120 ℃ the oven dry 6hr, the filter cake that obtains again with 70g CrO 3Mechanically mixing, granulation, in 250~400 ℃ of roasting 3hr, the material after the roasting is admixed 1~2% graphite, 5~15% water, is pressed into the tablet scavenging agent that gets product.

Claims (6)

1. the preparation method of a copper-bearing synthetic gas purifier, it waits to levy the Cu-Zn-Cr system that is, and its copper zinc chrome ratio is Cu: Zn: Cr=1: (0.5-3): (0.5-3); The preparation method is that the soluble copper salts solution of concentration 10-250g/l and the soluble Zn salts solution of concentration 10-250g/L carry out co-precipitation under the effect of concentration 5-20% precipitation agent, controlled temperature is at 65-85 ℃, control terminal point pH is 6.0-8.0, aging, the slurries filtration that obtains thus, washing, in 90-120 ℃ of oven dry 6hr, the filter cake that obtains again with compound mechanically mixing, the granulation of chromium, in 250-400 ℃ of roasting 3hr, material after the roasting is admixed 1~2% graphite, 5~15% water, is pressed into the tablet scavenging agent that gets product.
2. scavenging agent preparation method as claimed in claim 1, it is waited to levy and is that soluble copper salt is a nitrate.
3. scavenging agent preparation method as claimed in claim 1, it is waited to levy and is that soluble zinc salt is a nitrate.
4. scavenging agent preparation method as claimed in claim 1, it is waited to levy and is that precipitation agent is Na 2CO 3
5. scavenging agent preparation method as claimed in claim 1, it is waited to levy and is that precipitation agent is NaHCO 3
6. scavenging agent preparation method as claimed in claim 1, it waits to levy the compound that is chromium is CrO 3
CN 01127263 2001-09-26 2001-09-26 Prepn of copper-bearing synthetic gas purifier Expired - Fee Related CN1186249C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 01127263 CN1186249C (en) 2001-09-26 2001-09-26 Prepn of copper-bearing synthetic gas purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 01127263 CN1186249C (en) 2001-09-26 2001-09-26 Prepn of copper-bearing synthetic gas purifier

Publications (2)

Publication Number Publication Date
CN1344672A CN1344672A (en) 2002-04-17
CN1186249C true CN1186249C (en) 2005-01-26

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CN 01127263 Expired - Fee Related CN1186249C (en) 2001-09-26 2001-09-26 Prepn of copper-bearing synthetic gas purifier

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CN (1) CN1186249C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102390807A (en) * 2011-08-10 2012-03-28 西南化工研究设计院 Copper series purifying agent and preparation method thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010008857A1 (en) * 2010-02-22 2011-08-25 Lurgi GmbH, 60439 Process for the production of methanol

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102390807A (en) * 2011-08-10 2012-03-28 西南化工研究设计院 Copper series purifying agent and preparation method thereof

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CN1344672A (en) 2002-04-17

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Granted publication date: 20050126

Termination date: 20130926