CN103623839B - The Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene - Google Patents
The Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene Download PDFInfo
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- CN103623839B CN103623839B CN201210307816.XA CN201210307816A CN103623839B CN 103623839 B CN103623839 B CN 103623839B CN 201210307816 A CN201210307816 A CN 201210307816A CN 103623839 B CN103623839 B CN 103623839B
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- synthesizing chloroethylene
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Abstract
The invention discloses a kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, this catalyst comprises inert porous carrier and is carried on ruthenium salt, mantoquita and the nickel salt on described inert porous carrier, the quality of Ru accounts for 0.01 ‰ ~ 5%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:0.1 ~ 10:0.1 ~ 10.Reaction temperature can be reduced with catalyst acetylene hydrochlorination synthesizing chloroethylene of the present invention, make reaction temperature lower than 180 DEG C, and product is selective good, accessory substance is few, and reactivity is high, makes the conversion ratio of acetylene more than 99%, vinyl chloride is selective reaches 99.9%, catalyst strength of the present invention is high, and the life-span is long, and post catalyst reaction regeneration process is simple.Preparation method's technique simply, easily operates.
Description
Technical field
The present invention relates to one and utilize synthesizing chloroethylene by acetylene catalyst without mercury and preparation method.
Background technology
Along with the development of national economy and the raising day by day of living standards of the people, the demand of polyvinyl chloride is increasing.That applies in current carbide production vinyl chloride process contains mercury catalyst, can produce " mercury pollution " on the one hand, be faced with the problem of mercury scarcity of resources on the other hand.
At present, the research and development of acetylene hydrochlorination preparing chloroethylene catalyst without mercury are faced with activity and the life problems of catalyst.Currently used catalyst most active is poor, although the life-span of the active good catalyst had is shorter, cannot realize industrialization.For this reason, current research wishes that the method by Recompounded multielement and support modification improves the performance of catalyst more.
Summary of the invention
The object of the invention is to overcome the deficiencies in the prior art, a kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene is provided.
Technical scheme of the present invention is summarized as follows:
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprises inert porous carrier and is carried on ruthenium salt, mantoquita and the nickel salt on described inert porous carrier, the quality of Ru accounts for 0.01 ‰ ~ 5%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:0.1 ~ 10:0.1 ~ 10.
Described inert porous carrier is asphaltic base ball-type active carbon, opaque active carbon or cocoanut active charcoal.
Described ruthenium salt is that nitric acid ruthenium III, acetic acid ruthenium III, ruthenium trichloride, ruthenium sulfate III and pentachloro-monohydroxy close the sour potassium at least one of ruthenium IV.
Described mantoquita is copper nitrate II, Schweinfurt green II, copper chloride II, copper sulphate II and cupric phosphate II at least one.
Described nickel salt is Nickel Chloride, nickel nitrate II, nickelous sulfate II, nickel acetate II and dichloride hexamine nickel at least one.
Preferably the quality of Ru accounts for 0.01% ~ 1% of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene.Preferably 0.1% ~ 0.5%.
The mol ratio of Ru, Ni and Cu is preferably 1:0.5 ~ 5:0.5 ~ 5.
The invention has the advantages that: can reaction temperature be reduced with catalyst acetylene hydrochlorination synthesizing chloroethylene of the present invention, make reaction temperature lower than 180 DEG C, and product is selective good, accessory substance is few, and reactivity is high, makes the conversion ratio of acetylene more than 99%, vinyl chloride is selective reaches 99.9%, catalyst strength of the present invention is high, and the life-span is long, and post catalyst reaction regeneration process is simple.Preparation method's technique simply, easily operates.
Accompanying drawing explanation
Fig. 1 is evaluating catalyst schematic flow sheet of the present invention.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is further illustrated.
Embodiment 1
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprises asphaltic base ball-type active carbon and is carried on nitric acid ruthenium III, copper nitrate II and the Nickel Chloride on asphaltic base ball-type active carbon, the quality of Ru accounts for 0.3%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:3:3.
Embodiment 2
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprise asphaltic base ball-type active carbon and be carried on acetic acid ruthenium III on asphaltic base ball-type active carbon, Schweinfurt green II and copper chloride II, nickel nitrate that mass ratio is 1:1, the quality of Ru accounts for 0.1%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:1:5.
Embodiment 3
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprises the ruthenium trichloride and ruthenium sulfate III and copper sulphate II and nickelous sulfate that opaque active carbon and the mass ratio be carried on opaque active carbon are 1:1, the quality of Ru accounts for 0.5%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:5:1.
Embodiment 4
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprises opaque active carbon and is carried on ruthenium sulfate III, copper chloride II and the nickel acetate on opaque active carbon, the quality of Ru accounts for 0.01%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:0.1:10.
Embodiment 5
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprises cocoanut active charcoal and the pentachloro-monohydroxy be carried on cocoanut active charcoal closes dichloride hexamine nickel and the Nickel Chloride that the sour potassium of ruthenium IV, cupric phosphate II and mass ratio are 1:1, the quality of Ru accounts for 1%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:10:0.1.
Embodiment 6
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprise asphaltic base ball-type active carbon and be carried on acetic acid ruthenium III on asphaltic base ball-type active carbon, Schweinfurt green II and copper chloride II, nickel nitrate that mass ratio is 1:1, the quality of Ru accounts for 0.01 ‰, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:10:10.
Embodiment 7
A kind of Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, it comprises asphaltic base ball-type active carbon and is carried on nitric acid ruthenium III, copper nitrate II and the Nickel Chloride on asphaltic base ball-type active carbon, the quality of Ru accounts for 5%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:0.5:0.5.
The preparation of the catalyst of each embodiment above-mentioned can be prepared according to a conventional method.
Also can prepare by the method for embodiment 8 or embodiment 9:
Embodiment 8
1. asphaltic base ball-type active carbon (or opaque active carbon, cocoanut active charcoal) is dipped in dust technology, soaks 10h use water and rinse to neutral, dry 8h at 110 DEG C and carry out pretreatment;
2. ruthenium salt chloroazotic acid is made into wang aqueous solution; (ruthenium salt is selected from nitric acid ruthenium III, acetic acid ruthenium III, ruthenium trichloride, ruthenium sulfate III and pentachloro-monohydroxy and closes the sour potassium of ruthenium IV)
3. be dipped in the solution that 2. step prepare by 1. processing the inert porous carrier obtained through step, dipping 8h; Heating water bath evaporates to liquid, by solid in 160 DEG C of dryings 8 hours;
4. mantoquita and nickel salt being added concentration is be made into mixed solution in the aqueous hydrochloric acid solution of 1mol/L; (mantoquita is selected from copper nitrate II, Schweinfurt green II, copper chloride II, copper sulphate II and cupric phosphate II; Nickel salt is selected from Nickel Chloride, nickel nitrate II, nickelous sulfate II, nickel acetate II and dichloride hexamine nickel)
5. be dipped in by the product that 3. step obtains in the mixed solution that 4. step prepare, flood 8 hours, heating water bath evaporates to liquid, in 160 DEG C of dryings 8 hours, obtains the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene.
Embodiment 9
A preparation method for the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene, comprises the steps:
1. asphaltic base ball-type active carbon (or opaque active carbon, cocoanut active charcoal) is dipped in dust technology, soaks 8h, rinse to neutral with water, dry 6h at 120 DEG C and carry out pretreatment;
2. ruthenium salt, mantoquita and nickel salt being added concentration is be made into mixed solution in the aqueous hydrochloric acid solution of 1mol/L; (ruthenium salt closes the sour potassium of ruthenium IV from nitric acid ruthenium III, acetic acid ruthenium III, ruthenium trichloride, ruthenium sulfate III and pentachloro-monohydroxy; Mantoquita is selected from copper nitrate II, Schweinfurt green II, copper chloride II, copper sulphate II and cupric phosphate II; Nickel salt is selected from Nickel Chloride, nickel nitrate II, nickelous sulfate II, nickel acetate II and dichloride hexamine nickel)
3. be dipped in by the product that 1. step obtains in the mixed solution that 2. step prepare, flood 5 hours, heating water bath evaporates to liquid, puts into 110 DEG C, baking oven and dries 24 hours, obtain the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene.
Embodiment 10
The stainless steel fixed bed reactors utilizing internal diameter to be 10mm carry out performance evaluation to catalyst of the present invention.The device evaluated is shown in Fig. 1.
Hydrogen chloride 1(purity more than 96%) by pipeline successively through valve 3a, filter 4a, mass flowmenter 5a and one way stop peturn valve 6a;
Acetylene 2(purity more than 99%) by pipeline successively through valve 3b, filter 4b, mass flowmenter 5b and one way stop peturn valve 6b;
Enter after above-mentioned two strands of gas and vapor permeation in the stainless steel fixed bed reactors 8 that catalyst 9 of the present invention is housed, catalyst 9 loadings is 5ml, and tail gas stream adopts gas chromatograph analysis through surge tank 11 and absorption bottle 12 after alkali liquor absorption.Fid detector, GDX-301(2m × 3mm) packed column.
Filter 4a and 4b can remove the impurity such as sulphur, phosphorus, arsenic in unstripped gas stock.
Stainless steel fixed bed reactors adopt temperature controller temperature control, and the temperature in heating furnace 7 and stainless steel fixed bed reactors 8 is detected by thermocouple 10.
Wherein hydrogen chloride and acetylene flow rate ratio are 1.05.Reaction temperature is 150 DEG C.Utilize the apparatus and method of embodiment 10 to the evaluation of catalyst in table 1
Table 1
| Embodiment | Prepare the embodiment adopted | Conversion of alkyne % | Chloro ethylene yield % |
| 1 | 8 | 85 | 91 |
| 2 | 8 | 64 | 69 |
| 3 | 8 | 91 | 96 |
| 4 | 9 | 51 | 49 |
| 5 | 8 | 93 | 98 |
| 6 | 8 | 84 | 88 |
| 7 | 8 | 51 | 59 |
Claims (8)
1. the Ru-Ni-Cu catalyst of an acetylene hydrochlorination synthesizing chloroethylene, be made up of inert porous carrier and ruthenium salt, mantoquita and the nickel salt be carried on described inert porous carrier, the quality of Ru accounts for 0.01 ‰ ~ 5%, Ru of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene, the mol ratio of Ni and Cu is 1:0.1 ~ 10:0.1 ~ 10.
2. the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene according to claim 1, is characterized in that described inert porous carrier is asphaltic base ball-type active carbon, opaque active carbon or cocoanut active charcoal.
3. the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene according to claim 1, is characterized in that described ruthenium salt is that nitric acid ruthenium (III), acetic acid ruthenium (III), ruthenium trichloride, ruthenium sulfate (III) and pentachloro-monohydroxy close ruthenium (IV) sour potassium at least one.
4. the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene according to claim 1, is characterized in that described mantoquita is copper nitrate (II), Schweinfurt green (II), copper chloride (II), copper sulphate (II) and cupric phosphate (II) at least one.
5. the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene according to claim 1, is characterized in that described nickel salt is Nickel Chloride, nickel nitrate (II), nickelous sulfate (II), nickel acetate (II) and dichloride hexamine nickel at least one.
6. the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene according to claim 1, is characterized in that the quality of described Ru accounts for 0.01% ~ 1% of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene.
7. the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene according to claim 6, is characterized in that the quality of described Ru accounts for 0.1% ~ 0.5% of the Ru-Ni-Cu catalyst quality of described acetylene hydrochlorination synthesizing chloroethylene.
8. the Ru-Ni-Cu catalyst of acetylene hydrochlorination synthesizing chloroethylene according to claim 1, is characterized in that the mol ratio of described Ru, Ni and Cu is 1:0.5 ~ 5:0.5 ~ 5.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107456990A (en) * | 2017-08-29 | 2017-12-12 | 贵州重力科技环保有限公司 | A kind of high degree of dispersion ruthenium-based catalyst of acetylene hydrochlorination and preparation method thereof |
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| CN101670293A (en) * | 2009-03-06 | 2010-03-17 | 清华大学 | Method for synthesizing and regenerating mercury-free catalyst for hydrochlorination of acetylene and application thereof |
| CN101947465A (en) * | 2010-09-03 | 2011-01-19 | 清华大学 | Mercury-free catalyst with low bullion content for acetylene hydrochlorination and application thereof |
| CN102259007A (en) * | 2011-06-07 | 2011-11-30 | 李伟 | Method for preparing mercury-free catalyst for synthesis of chloroethylene by acetylene process |
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| FR2910350B1 (en) * | 2006-12-22 | 2009-01-30 | Solvay | CATALYTIC HYDROCHLORIZATION SYSTEM AND PROCESS FOR PRODUCING VINYL CHLORIDE FROM ACETYLENE AND HYDROGEN CHLORIDE IN THE PRESENCE OF THIS CATALYTIC SYSTEM |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101670293A (en) * | 2009-03-06 | 2010-03-17 | 清华大学 | Method for synthesizing and regenerating mercury-free catalyst for hydrochlorination of acetylene and application thereof |
| CN101947465A (en) * | 2010-09-03 | 2011-01-19 | 清华大学 | Mercury-free catalyst with low bullion content for acetylene hydrochlorination and application thereof |
| CN102259007A (en) * | 2011-06-07 | 2011-11-30 | 李伟 | Method for preparing mercury-free catalyst for synthesis of chloroethylene by acetylene process |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107456990A (en) * | 2017-08-29 | 2017-12-12 | 贵州重力科技环保有限公司 | A kind of high degree of dispersion ruthenium-based catalyst of acetylene hydrochlorination and preparation method thereof |
| CN107456990B (en) * | 2017-08-29 | 2020-07-17 | 贵州重力科技环保有限公司 | High-dispersity ruthenium-based catalyst for acetylene hydrochlorination and preparation method thereof |
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