CN108246277A - One kind efficiently synthesizes trifluoroiodomethane method - Google Patents
One kind efficiently synthesizes trifluoroiodomethane method Download PDFInfo
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- CN108246277A CN108246277A CN201810235825.XA CN201810235825A CN108246277A CN 108246277 A CN108246277 A CN 108246277A CN 201810235825 A CN201810235825 A CN 201810235825A CN 108246277 A CN108246277 A CN 108246277A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/361—Preparation of halogenated hydrocarbons by reactions involving a decrease in the number of carbon atoms
- C07C17/363—Preparation of halogenated hydrocarbons by reactions involving a decrease in the number of carbon atoms by elimination of carboxyl groups
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
- B01J23/04—Alkali metals
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Abstract
The invention discloses one kind to efficiently synthesize trifluoroiodomethane method, by CF3COOH steam and iodine vapor, under catalyst action, reaction generation trifluoroiodomethane;The catalyst is using activated carbon or graphene as carrier loaded 1~10wt%KNO3With 2~7wt%RbNO3Catalyst;Then NaOH solution, silica gel and molecular sieve are passed sequentially through to effectively remove CF3Thus impurity and moisture in I efficiently collect high-purity C F3I products.The method has that reaction rate is fast, selectivity is good, yield is high, reactant utilization rate is high, energy saving, is expected to realization industrialized production, meets the current market demand.
Description
Technical field
The present invention relates to one kind to efficiently synthesize trifluoroiodomethane method.
Background technology
Trifluoroiodomethane (CF3I greenhouse effects) are dived value (GWP) < 5, and ozone depletion value (ODP) of diving is 0, is combined
State is classified as the major components of the 3rd generation environmental protection refrigerant.Other than it can be used as new gas extinguishing chemical and refrigerant, in fluorine-containing centre
Other fields such as body, conductor etching, foaming agent also have wide practical use.
CF3I document reports CF3I synthesis technologies are numerous, and main method has:
(1) perfluorocarboxylic acid salt pyrolysismethod:With CF3COM (M=Ag, Na, K, Hg, Pb, Ba) and iodine (I2) it is raw material, in strong pole
Property solvent in heat resolve prepare CF3I, this is also to be suggested the synthetic method with industrialization and practical value earliest,
(J.Am.Chem.Soc.1950(72):584-587.3806-7 J.Chem.Soc., 1951 (2):584-587.).Wherein with silver
The pyrolysis yield of salt is higher but expensive.The discoveries such as Paskovich, sodium salt or sylvite flow back in dimethylformamide (DMF)
Under, CF can be improved3I yields are to 70% or so, (J.Org.Chem., 1967,32 (3):833-835.).Xu Huatang etc. is with ring fourth
It is solvent that sulfone, which substitutes DMF, obtains CF3The yield of I is 80% or so, (chemical reagent, 1989,11 (2):123.).
(2) fluoroform iodide process:Japan Patent JP52068110 is reported with fluoroform (CF3) and I H2It is living for raw material
Property charcoal carrying alkali metal or alkaline-earth metal be catalyst preparation CF3I.Catalyst shows preferable catalytic activity, due to reaction
Temperature is high, and catalyst carbon deposition is serious, and the service life is shorter, and the high polymer generated increases and recycles unreacted I2Difficulty.
(3) it is proposed in French Patent (FRP) FR2794456 with pentafluoroethane (C2F5) and I H2For the synthetic route of raw material, the technique
With the catalyst system and catalyzing similar with fluoroform iodide process, unstripped gas is catalyzed by activated carbon supported alkali or alkaline earth metal
Agent bed can obtain CF3I。
In conclusion existing preparation CF3There are expensive raw material prices, of high cost for the method for I, and reaction dissolvent consumption is big, production
The a series of problems such as object yield is low, poor selectivity, raw material availability are low.Therefore, find one it is easy to operate, high selectivity
CF3I synthetic routes are most important.
Invention content
To solve the above-mentioned problems, the purpose of the present invention is to provide a kind of synthesis easy to operate, selectivity of product is high
CF3The method of I.In order to achieve the above object, the invention is realized by the following technical scheme:
One kind efficiently synthesizes CF3The method of I, CF3COOH steam and iodine vapor, under catalyst action, reaction generation trifluoro
Iodomethane;
The catalyst is using activated carbon or graphene as carrier loaded 1~10wt%KNO3With 2~7wt%RbNO3Urge
Agent;CF3The molar ratio of COOH steam and iodine vapor is 1:1~2:1;Reaction temperature is 450-550 DEG C;Reaction time is 10-
15min;CF3The flow of COOH steam is 10-20mL/min.
Catalyst is synthesized KNO3And RbNO3It is dissolved in water, adds in activated carbon or graphene thereto, be ultrasonically treated
30min is stood overnight;Filtering, 5h is dried by Solid separate at 100 DEG C, then 500 DEG C of calcinings under high pure nitrogen atmosphere
Catalyst is made in 2h.KNO3And RbNO3It is 3-8g/500ml with water consumption ratio.
Further, in the above-mentioned technical solutions, obtained trifluoroiodomethane is passed through the first collector, the second receipts successively
Storage, caustic treater, drier and absorber remove impurity and moisture content;It is heated outside first collector using recirculated water;Alkali cleaning
The lye of tank is NaOH solution;Drier in drier is silica gel;Adsorbent in absorber is molecular sieve.
Further, in the above-mentioned technical solutions, the temperature of level-one collector outer circulation water is 70-80 DEG C;In caustic treater
A concentration of 0.1-5% of NaOH solution;Adsorbent is 5A molecular sieves in absorber.
Further, in the above-mentioned technical solutions, trifluoroiodomethane is received using cold-trap.
Further, in the above-mentioned technical solutions, the temperature for collecting trifluoroiodomethane cold-trap is -70 DEG C.
Further, in the above-mentioned technical solutions, CF3COOH steam is to be vaporized to generate by the vaporizer that temperature is 100 DEG C;
Iodine vapor is generated by the iodine evaporator that temperature is 200 DEG C.
Further, in the above-mentioned technical solutions, trifluoroiodomethane method is efficiently synthesized, reaction unit includes reactor,
The reactor inlet connects CF3COOH vaporizers and iodine evaporator;The reactor outlet is sequentially connected the first collector,
Two collectors, caustic treater, drier, absorber, cold-trap.
It is provided by the present invention to efficiently synthesize CF3I methods are using activated carbon or graphene as carrier loaded 1~10wt%
KNO3With 2~7wt%RbNO3As catalyst, make CF3COOH steam and iodine vapor chemically react in high-temperature reactor
And generate CF3Then I passes sequentially through NaOH solution, silica gel and molecular sieve to effectively remove CF3Impurity and moisture in I, thus
The CF of synthesis3The yield of I is up to 90%, since catalyst selects matters, and processing step reasonable design, can not only accelerate
Reaction rate improves yield, energy saving so as to improve the utilization rate of reactant, is expected to realize industrialized production, so as to
Meet the current market demand.
Description of the drawings
Fig. 1 is the flow chart provided by the invention for efficiently synthesizing trifluoroiodomethane method.
Case is embodied
Embodiment 1
1st, synthetic catalyst:By 3.0g KNO3With 5g RbNO3It is dissolved in 500mL water, adds in 100g activity thereto
Charcoal is ultrasonically treated 30min, stands overnight;Filtering, dries 5h, then in high pure nitrogen atmosphere by Solid separate at 100 DEG C
Lower 500 DEG C of calcinings 2h, is made catalyst.
2nd, CF is synthesized3I
(1)CF3COOH steam and iodine vapor in molar ratio 1:1 enters 500 DEG C of reactors, is catalyzed in reactor equipped with 100g
Agent controls CF3The flow of COOH steam is 20mL/min, CF3The reaction time of COOH and iodine generates CF for 10min3I。
(2) make above-mentioned CF3I gases are passed through the first collector, the second collector, caustic treater, drier and absorber successively,
Remove H2O、CO2, the impurity such as HF.It is recycled outside level-one collector using 80 DEG C of water;Lye in caustic treater is 0.5%NaOH
Solution;Drier in drier is silica gel;Adsorbent in absorber is 5A molecular sieves.Finally by -70 DEG C of cold-trap pair
CF3I solution is received, CF3The yield of I is 84.6%.
Embodiment 2
1st, synthetic catalyst:By 7.0g KNO3With 0.7g RbNO3It is dissolved in 500mL water, adds in 100g graphite thereto
Alkene is ultrasonically treated 30min, stands overnight;Filtering, dries 5h, then in high pure nitrogen atmosphere by Solid separate at 100 DEG C
Lower 500 DEG C of calcinings 2h, is made catalyst.
2nd, CF is synthesized3I
(1)CF3COOH steam and iodine vapor in molar ratio 2:1 enters 550 DEG C of reactors, is catalyzed in reactor equipped with 100g
Agent controls CF3The flow of COOH steam is 20mL/min, CF3The reaction time of COOH and iodine generates CF for 10min3I。
(2) make above-mentioned CF3I gases are passed through the first collector, the second collector, caustic treater, drier and absorber successively,
Remove H2O、CO2, the impurity such as HF.It is recycled outside level-one collector using 80 DEG C of water;Lye in caustic treater is 0.5%NaOH
Solution;Drier in drier is silica gel;Adsorbent in absorber is 5A molecular sieves.Finally by -70 DEG C of cold-trap pair
CF3I solution is received, CF3The yield of I is 90.7%.
Claims (7)
1. one kind efficiently synthesizes trifluoroiodomethane method, it is characterised in that:
CF3COOH steam and iodine vapor, under catalyst action, reaction generation trifluoroiodomethane;
The catalyst is using activated carbon or graphene as carrier loaded 1~10wt%KNO3With 2~7wt%RbNO3Catalysis
Agent;CF3The molar ratio of COOH steam and iodine vapor is 1:1~2:1;Reaction temperature is 450-550 DEG C;Reaction time is 10-
15min;CF3The flow of COOH steam is 10-20mL/min.
2. trifluoroiodomethane method is efficiently synthesized according to claim 1, it is characterised in that:By obtained trifluoroiodomethane according to
It is secondary to be passed through the first collector, the second collector, caustic treater, drier and absorber, remove impurity and moisture content;Outside first collector
It is heated using recirculated water;The lye of caustic treater is NaOH solution;Drier in drier is silica gel;Suction in absorber
Attached dose is molecular sieve.
3. according to claim 2 efficiently synthesize trifluoroiodomethane method, it is characterised in that:Level-one collector outer circulation water
Temperature be 70-80 DEG C;A concentration of 0.1-5% of NaOH solution in caustic treater;Adsorbent is 5A molecular sieves in absorber.
4. trifluoroiodomethane method is efficiently synthesized according to claim 2, it is characterised in that:Using cold-trap to trifluoroiodomethane
It is received.
5. according to claim 4 efficiently synthesize trifluoroiodomethane method, it is characterised in that:Collect trifluoroiodomethane cold-trap
Temperature be -70 DEG C.
6. efficiently synthesize trifluoroiodomethane method according to Claims 1 to 5 any one, it is characterised in that:CF3COOH
Steam is to be vaporized to generate by the vaporizer that temperature is 100 DEG C;Iodine vapor is generated by the iodine evaporator that temperature is 200 DEG C.
7. according to claim 6 efficiently synthesize trifluoroiodomethane method, it is characterised in that:Reaction unit includes reaction
Device, the reactor inlet connect CF3COOH vaporizers and iodine evaporator;The reactor outlet is sequentially connected the first collection
Device, the second collector, caustic treater, drier, absorber, cold-trap.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020180831A1 (en) * | 2019-03-04 | 2020-09-10 | Honeywell International Inc. | Processes for producing trifluoroiodomethane using trifluoroacetic acid |
CN113316563A (en) * | 2018-12-21 | 2021-08-27 | 霍尼韦尔国际公司 | Catalyst and integrated process for producing trifluoroiodomethane |
CN113423681A (en) * | 2019-02-18 | 2021-09-21 | 霍尼韦尔国际公司 | One-step process for making trifluoroiodomethane from trifluoroacetyl halide, hydrogen and iodine |
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CN101412657A (en) * | 2006-10-16 | 2009-04-22 | 霍尼韦尔国际公司 | Catalyst promoter for producing trifluoroiodomethane and pentafluoroiodoethane |
CN101481291A (en) * | 2007-11-28 | 2009-07-15 | 霍尼韦尔国际公司 | Method for pretreating and regenerating catalysts used in a process for making fluoroiodoalkanes |
CN102992943A (en) * | 2011-09-14 | 2013-03-27 | 中化蓝天集团有限公司 | Trifluoroiodomethane preparation method |
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CN101412657A (en) * | 2006-10-16 | 2009-04-22 | 霍尼韦尔国际公司 | Catalyst promoter for producing trifluoroiodomethane and pentafluoroiodoethane |
CN101481291A (en) * | 2007-11-28 | 2009-07-15 | 霍尼韦尔国际公司 | Method for pretreating and regenerating catalysts used in a process for making fluoroiodoalkanes |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN113316563A (en) * | 2018-12-21 | 2021-08-27 | 霍尼韦尔国际公司 | Catalyst and integrated process for producing trifluoroiodomethane |
JP2022514671A (en) * | 2018-12-21 | 2022-02-14 | ハネウェル・インターナショナル・インコーポレーテッド | Catalyst and integration process for producing trifluoroiodomethane |
CN113423681A (en) * | 2019-02-18 | 2021-09-21 | 霍尼韦尔国际公司 | One-step process for making trifluoroiodomethane from trifluoroacetyl halide, hydrogen and iodine |
WO2020180831A1 (en) * | 2019-03-04 | 2020-09-10 | Honeywell International Inc. | Processes for producing trifluoroiodomethane using trifluoroacetic acid |
US10941089B2 (en) | 2019-03-04 | 2021-03-09 | Honeywell International Inc. | Processes for producing trifluoroiodomethane using trifluoroacetic acid |
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