CN1463793A - Ferromanganese catalyst for Fischer-Tropsch synthesis and method for preparing the same - Google Patents
Ferromanganese catalyst for Fischer-Tropsch synthesis and method for preparing the same Download PDFInfo
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- CN1463793A CN1463793A CN 02121248 CN02121248A CN1463793A CN 1463793 A CN1463793 A CN 1463793A CN 02121248 CN02121248 CN 02121248 CN 02121248 A CN02121248 A CN 02121248A CN 1463793 A CN1463793 A CN 1463793A
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- 239000003054 catalyst Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title abstract description 12
- 230000015572 biosynthetic process Effects 0.000 title abstract description 5
- 238000003786 synthesis reaction Methods 0.000 title abstract description 5
- 229910000616 Ferromanganese Inorganic materials 0.000 title 1
- DALUDRGQOYMVLD-UHFFFAOYSA-N iron manganese Chemical compound [Mn].[Fe] DALUDRGQOYMVLD-UHFFFAOYSA-N 0.000 title 1
- 238000006243 chemical reaction Methods 0.000 claims abstract description 17
- 239000002243 precursor Substances 0.000 claims abstract description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 50
- 239000011572 manganese Substances 0.000 claims description 30
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 24
- 229910052748 manganese Inorganic materials 0.000 claims description 22
- 229910052742 iron Inorganic materials 0.000 claims description 21
- 239000000243 solution Substances 0.000 claims description 20
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 17
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 16
- 238000002360 preparation method Methods 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 14
- 229910052700 potassium Inorganic materials 0.000 claims description 14
- 239000008367 deionised water Substances 0.000 claims description 12
- 229910021641 deionized water Inorganic materials 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 229910000027 potassium carbonate Inorganic materials 0.000 claims description 11
- 235000011181 potassium carbonates Nutrition 0.000 claims description 11
- 239000012266 salt solution Substances 0.000 claims description 10
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims description 8
- 229910021529 ammonia Inorganic materials 0.000 claims description 8
- 239000012065 filter cake Substances 0.000 claims description 8
- 239000011591 potassium Substances 0.000 claims description 8
- 238000010009 beating Methods 0.000 claims description 6
- 229910052791 calcium Inorganic materials 0.000 claims description 6
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 239000002002 slurry Substances 0.000 claims description 6
- 239000002244 precipitate Substances 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000011575 calcium Substances 0.000 claims description 4
- 229910002651 NO3 Inorganic materials 0.000 claims description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 3
- MVFCKEFYUDZOCX-UHFFFAOYSA-N iron(2+);dinitrate Chemical compound [Fe+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MVFCKEFYUDZOCX-UHFFFAOYSA-N 0.000 claims description 3
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 238000000748 compression moulding Methods 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims description 2
- 229940071125 manganese acetate Drugs 0.000 claims description 2
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 claims description 2
- 229920001296 polysiloxane Polymers 0.000 claims description 2
- 238000000247 postprecipitation Methods 0.000 claims description 2
- 235000015320 potassium carbonate Nutrition 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 238000001556 precipitation Methods 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 8
- 230000008901 benefit Effects 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 11
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 8
- 239000010703 silicon Substances 0.000 description 8
- 229910052710 silicon Inorganic materials 0.000 description 8
- 229910052799 carbon Inorganic materials 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 230000032683 aging Effects 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 238000005303 weighing Methods 0.000 description 4
- 239000004215 Carbon black (E152) Substances 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 3
- 239000012752 auxiliary agent Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- AEMRFAOFKBGASW-UHFFFAOYSA-M Glycolate Chemical compound OCC([O-])=O AEMRFAOFKBGASW-UHFFFAOYSA-M 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 210000003739 neck Anatomy 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
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- Catalysts (AREA)
Abstract
The catalyst for Fischer-Tropsch synthesis has the atom makeup of Fe 100, Mn 4-100, Ca 2-50 and K 0.2-10; and is prepared with precursors and through precipitation process. The present invention has the advantages of large specific surface area, high strengthen, low cost, high conversion rate and high selectivity.
Description
Technical field:
The present invention relates to a kind of iron/manganese catalyst and preparation method thereof, concrete is exactly a kind of Fischer-Tropsch synthetic iron/manganese catalyst and preparation method thereof that is used for.
Background technology:
Ferrum-based catalyst is a most frequently used class fischer-tropsch synthetic catalyst, is the Fischer-Tropsch synthesis of raw material because of it has the active coal based synthetic gas that is specially adapted to low hydrogen-carbon ratio of higher water-gas shift.That successfully realize at present catalyzer that the Sasol company in the South Africa of the synthetic heavy industrialization operation of Fischer-Tropsch adopts is exactly ferrum-based catalyst (M.E.Dry et al, Catalysis Today, 1990,6 (3) 183-206).
Van Dijk, Jenson, people such as Maiti (Applied Catalyst, 1982,2,273-298; J ofCatalysts, 1985,92,98-108; Applied Catalyst, 1982,16 (2), 215-225) and people (Ind.Eng.Chem.Process Des.Dev.1983 such as Arakawa, 22,97-103) at length studied the active and optionally influence of manganese auxiliary agent and potassium promoter respectively, thought that an amount of potassium, manganese auxiliary agent can assist to improve selectivity of catalyst, the raising activity of such catalysts iron-base fischer-tropsch synthesis catalyst.Some other auxiliary agent people have also been done the research of some.(US patent 5,118,715 for people such as the Iglesia of Exxon research engineering company and Fiato, US Patent 4,621,102) adopt interpolation copper to improve selectivity of catalyst, but this catalyst activity is not very high, is 1000h at 275 ℃, 2.0MPa, air speed
-1, unstripped gas H
2/ CO only is 50% than the transformation efficiency that is 2 o'clock CO, and the glycolate that adopts iron, manganese is as by raw material, and the preparation procedure complexity, and the Preparation of Catalyst cost is higher.In Shanxi Coal-Chemical Inst., Chinese Academy of Sciences's exploitation two-stage method synthetic gasoline technology, the catalyzer that uses is iron/manganese Ultra-fine Particle Catalysts of adopting the control degradation method to make (granted patent number: CN1137 058A), this catalyzer has higher Fischer-Tropsch composite reactive, reach target product selectivity preferably, but its production cost is higher, and the physical strength of catalyzer is also not so good.About the interpolation of structural promoter, people also have some researchs, but adopt loaded catalyst mostly, and carrier is generally SiO
2, Al
2O
3Deng.People such as Rao have announced the patent (US Patent4,340,503) of the supported ferric catalyst that contains potassium promoter, SiO
2Be carrier, the charge capacity of iron is 5-25%wt, but this catalyst selectivity is relatively poor, at 280 ℃, 1000h
-1, 2.0MPa, unstripped gas H
2/ CO ratio is 2.0 o'clock C
2-4 =/ C
2-4 0Ratio only be 0.5, and the weight selectivity of methane is up to 18.6-25.5%, C
5 +The weight selectivity also only be 41.8-45.6%.
Summary of the invention:
The purpose of this invention is to provide a kind of high reactivity and have high low-carbon alkene and C
5 +The hydrocarbon product selectivity, physical strength is good, synthetic iron/manganese catalyst of Fischer-Tropsch that cost is low and preparation method thereof.
The atomic ratio of Fe, Mn, Ca, K is in the catalyzer of the present invention:
Fe∶Mn∶Ca∶K＝100∶4-100∶2-50∶0.2-10
SiO wherein
2Weight percent in catalyzer is 1-45wt%.
Active constituent Fe, Mn, Ca, K exist with oxide form respectively in the catalyzer.
Preparation method of the present invention comprises the steps:
(1) by the composition of above-mentioned catalyzer, precursor iron nitrate, nitrocalcite, manganous nitrate or manganese acetate that catalyzer is formed are mixed with the mixing salt solution that concentration is the 0.05-2.0 mol;
(2) being the ammonia soln of 0.1-5.0 mol with mixing salt solution and the concentration for preparing, is 30-90 ℃ in temperature of reaction, stirs under the condition of pH=7.0-11.5, precipitates, and post precipitation left standstill 5-48 hour, filters, and gets filter cake;
(3) press the content that catalyzer is formed potassium, its precursor salt of wormwood is made into the solution of potassium carbonate that concentration is the 0.1-1.5 mol;
(4) contain SiO by silicone content in the catalyzer composition to the filter cake adding
2The silica aqueous solution of 25wt%, add simultaneously solution of potassium carbonate and with the weight ratio of preformed catalyst be deionized water: preformed catalyst=5-9: 1 deionized water, mix making beating;
(5) slurries were dried 5-60 hour in 40-95 ℃ of water-bath, and dried 6-42 hour in 80-150 ℃ dry back again, then in 300-650 ℃ of following roasting 1-12 hour, and cooling, compression molding.
The atomic ratio of Fe, Mn, Ca, K the best is Fe: Mn: Ca: K=100: 5-30: 3-20: 1-5, wherein SiO in the aforesaid catalyzer
2Weight percent in catalyzer is 5-25wt%.
The concentration of aforesaid mixing salt solution is preferably the 0.10-1.00 mol.
The optimum concn of aforesaid ammoniacal liquor is the 0.5-3.0 mol.
Aforesaid temperature of reaction is preferably 55-90 ℃, and the pH during reaction is preferably pH=7.5-11.0.
SiO in the aforesaid catalyzer
2Content is preferably 5-25wt%.
Aforesaid solution of potassium carbonate concentration is preferably the 0.2-1.0 mol.
The activation condition of catalyzer of the present invention is: 0.1-2.0MPa, 500-4000h
-1, 200-400 ℃ condition under with hydrogen, carbon monoxide or H
2/ CO reduced 12-60 hour than the synthetic gas for 0.5-3.0.
The working conditions of catalyzer of the present invention when Fischer-Tropsch is synthetic is: 230-380 ℃, 500-5000h
-1, 2.50MPa, unstripped gas H
2/ CO is 0.5-3.0.
The present invention compares with existing catalyzer has following advantage:
(1) has big specific surface area and high physical strength;
(2) be raw material with iron nitrate, manganous nitrate and nitrocalcite and add solution of potassium carbonate and silicon sol simultaneously, greatly the Preparation of Catalyst program, reduced the Preparation of Catalyst cost and simplified;
(3) this catalyzer after pre-treatment, can be realized the steady running of high-speed high conversion under above-mentioned test conditions under above-mentioned pretreatment condition;
(4) keeping the highly active while, this catalyzer has high low-carbon alkene and C
5 +Hydrocarbon-selective and low methane selectively;
(5) this catalyzer not only had been applicable to the coal based synthetic gas of low hydrogen-carbon ratio but also had been applicable to the Sweet natural gas base synthetic gas of high hydrogen-carbon ratio.
Embodiment:
Embodiment one:
Take by weighing Fe (NO
3)
39H
2The O620.0 gram, the Mn (NO of 50%wt
3)
2Solution 45.1 grams, Ca (NO
3)
24H
2The O54.5 gram is mixed with the mixing solutions that total concn is 0.9 mol with deionized water, and mixing salt solution places 90 ℃ of water-bath preheatings, and compound concentration is the ammonia soln of 0.50 mol, preheating in 60 ℃ of water-baths.100mL in advance packs in the low flask of four necks circle, pH value is 9 ammonia soln, round-bottomed flask is immersed in 90 ℃ of water-baths, simultaneously slowly be added dropwise in the flask above-mentioned ammonia soln and salts solution in the whipping process, it is 90 ℃ that whole precipitation process all keeps system temperature, pH value is 9.0, and the precipitation process time spent is about 1 hour.After precipitation is finished, left standstill aging 15 hours, filter.Directly add simultaneously 31.0 gram silicon sol (SiO in the filter cake
2Weight percentage is 5.0%), the 700mL deionized water, and 60mL concentration is the solution of potassium carbonate of 0.32 mol, making beating.Slurries are evaporate to dryness (48 hours times spent) in 80 ℃ of water-baths.Dried 12 hours down at 120 ℃ then, at last 500 ℃ of following roastings 5 hours.The cooling back is at the 60.0MPa lower sheeting, and moulding is ground into the 20-40 order.In 0.20MPa, air speed is 1000h
-1, use H under 250 ℃ of conditions
2/ CO atomic ratio is 2.0 synthetic gas reduction 36 hours, is 1000-3000h at 250-280 ℃, air speed then
-1, 2.50MPa, unstripped gas H
2/ CO is used for fixing the Fischer-Tropsch synthesis performance that bed bioreactor is estimated this catalyzer than under the condition of 0.67-3.0.The atomic ratio of this catalyzer each component is 100Fe: 8Mn: 15Ca: 2.5K: 8SiO
2, reaction result sees Table one.
Embodiment two:
As described in embodiment one, take by weighing Fe (NO
3)
39H
2The O620.0 gram, the Mn (NO of 50%wt
3)
2Solution 140.0 grams, Ca (NO
3)
24H
2The O11.0 gram is mixed with the mixing solutions that total concn is 0.2 mol with deionized water, and mixing salt solution places 75 ℃ of water-bath preheatings, and compound concentration is the ammonia soln of 2.7 mol, preheating in 60 ℃ of water-baths.Press embodiment one described intermediate processing at 75 ℃, PH precipitates under 8.0 the condition, and the precipitation process time spent is about 0.8 hour.After precipitation is finished, left standstill aging 12 hours, filter.Add 64 gram silicon sol (SiO in the silicon sol in the gained filter cake simultaneously
2Weight percentage is 9.5%), the 750mL deionized water, and 10mL concentration is the solution of potassium carbonate of 0.75 mol, making beating.Slurries are evaporate to dryness (48 hours times spent) in 85 ℃ of water-baths.Dried 12 hours down at 120 ℃ then, at last 500 ℃ of following roastings 5 hours.The cooling back is at the 60.0MPa lower sheeting, and moulding is ground into the 20-40 order.The atomic ratio of this catalyzer each component is 100Fe: 25Mn: 3Ca: 1K: 17SiO
2, reduction and reaction conditions such as embodiment one.Reaction result sees Table one.
Embodiment three:
As described in embodiment one, take by weighing Fe (NO
3)
39H
2The O620.0 gram, the Mn (NO of 50%wt
3)
2Solution 80.0 grams, Ca (NO
3)
24H
2The O29.0 gram is mixed with the mixing solutions that total concn is 0.6 mol with deionized water, and mixing salt solution places 55 ℃ of water-bath preheatings, and compound concentration is the ammonia soln of 2.0 mol, preheating in 50 ℃ of water-baths.Press embodiment one described intermediate processing at 55 ℃, PH precipitates under 8.5 the condition, and the precipitation process time spent is about 0.8 hour.After precipitation is finished, left standstill aging 16 hours, filter.Add 102.35 gram silicon sol (SiO in the silicon sol in the gained filter cake simultaneously
2Weight percentage is 15%), the 850mL deionized water, and 46mL concentration is the solution of potassium carbonate of 0.75 mol, making beating.Slurries are evaporate to dryness (50 hours times spent) in 80 ℃ of water-baths.Dried 12 hours down at 120 ℃ then, at last 500 ℃ of following roastings 5 hours.The cooling back is at the 60.0MPa lower sheeting, and moulding is ground into the 20-40 order.The atomic ratio of this catalyzer each component is 100Fe: 14.5Mn: 8.0Ca: 4.2K: 27.6SiO
2, reduction and reaction conditions such as embodiment one.Reaction result sees Table one.
Embodiment four:
As described in embodiment one, take by weighing Fe (NO
3)
39H
2The O620.0 gram, the Mn (NO of 50%wt
3)
280.0 the solution gram, Ca (NO
3)
24H
2The O42.0 gram is mixed with the mixing solutions that total concn is 0.6 mol with deionized water, and mixing salt solution places 60 ℃ of water-bath preheatings, and compound concentration is ammonia soln preheating in 50 ℃ of water-baths of 1.5 mol.Press embodiment one described intermediate processing at 55 ℃, PH precipitates under 11.0 the condition, and the precipitation process time spent is about 1.2 hours.After precipitation is finished, left standstill aging 16 hours, filter.The gained filter cake adds 145 gram silicon sol (SiO in the silicon sol simultaneously
2Weight percentage is 20%), the 850mL deionized water, and 39mL concentration is the solution of potassium carbonate of 0.30 mol, making beating.Slurries are evaporate to dryness (52 hours times spent) in 75 ℃ of water-baths.Dried 12 hours down at 120 ℃ then, at last 500 ℃ of following roastings 5 hours.The cooling back is at the 60.0MPa lower sheeting, and moulding is ground into the 20-40 order.The atomic ratio of this catalyzer each component is 100Fe: 14.5Mn: 11.5Ca: 1.5K: 39SiO
2, reduction and reaction conditions such as embodiment one.Reaction result sees Table one.
Comparative Examples
People such as Rao have announced the patent (US Patent4,340,503) of the supported ferric catalyst that contains potassium promoter, SiO
2Be carrier, the charge capacity of iron is 14.1%wt, at 280 ℃, 1000h
-1, 2.0MPa, unstripped gas H
2/ CO ratio is 2.0 to react, and reaction result sees Table one.
Table one: the reactivity worth of each catalyzer and selectivity of product catalyzer embodiment one embodiment two embodiment three embodiment four Comparative Examples thereof among the embodiment
*Temperature of reaction/
270 280 280 270 280 280 270 270 270 270 270 280 280 ℃ of H
2/ CO 1.0 2.0 2.0 2.0 2.0 1.0 2.0 2.0 1.0 2.0 1.0 1.5 1.3 air speed h
-11,000 2,000 3,000 1,000 2,000 1,000 1,000 2,000 2,000 1,000 2,000 3000 1000CO transformation efficiencys, 83.85 86.84 80.93 77.90 89.26 96.66 95.71 93.06 95.97 95.32 93.12 92.19-%CO
2Selectivity 34.93 35.08 36.25 27.12 32.82 38.75 27.95 29.55 40.21 34.57 43.25 40.23-% hydrocarbon distribution wt%C
16.43 9.45 8.05 9.66 12.11 9.40 7.73 7.24 6.32 7.32 5.69 7.02 25.5C
2-428.73 34.78 32.88 23.08 23.67 38.10 19.68 22.31 20.53 18.80 19.19 16.55 28.9C
5 +64.84 55.77 59.07 67.26 64.22 61.90 72.59 70.45 73.15 73.88 75.12 76.43 45.6 ethylenic alkoxy rate C
2-4 =/ C
2-4 03.96 2.68 2.85 3.22 2.85 3.86 3.44 3.33 4.45 3.52 4.13 3.67 0.45
*People such as Rao have announced the synthetic result (US Patent 4,340,503) of Fischer-Tropsch of the load typed iron catalyst that contains potassium promoter of potassium promoter
Claims (8)
1. one kind is used for Fischer-Tropsch synthetic iron/manganese catalyst, it is characterized in that the atomic ratio of Fe in the catalyzer, Mn, Ca, K is: Fe: Mn: Ca: K=100: 4-100: 2-50: 0.2-10
SiO wherein
2Weight percent in catalyzer is 1-45wt%; Active constituent Fe, Mn, Ca, K exist with oxide form respectively in the catalyzer.
2. a kind of preparation method who is used for Fischer-Tropsch synthetic iron/manganese catalyst as claimed in claim 1 is characterized in that the preparation method comprises the steps:
(1) press the composition of catalyzer, precursor iron nitrate, nitrocalcite, manganous nitrate or manganese acetate that catalyzer is formed are mixed with the mixing salt solution that concentration is the 0.05-2.0 mol;
(2) being the ammonia soln of 0.1-5.0 mol with mixing salt solution and the concentration for preparing, is 30-90 ℃ in temperature of reaction, stirs under the condition of pH=7.0-11.5, precipitates, and post precipitation left standstill 5-48 hour, filters, and gets filter cake;
(3) press the content that catalyzer is formed potassium, its precursor salt of wormwood is made into the solution of potassium carbonate that concentration is the 0.1-1.5 mol;
(4) contain SiO by silicone content in the catalyzer composition to the filter cake adding
2The silica aqueous solution of 25wt%, add simultaneously solution of potassium carbonate and with the weight ratio of preformed catalyst be deionized water: preformed catalyst=5-9: 1 deionized water, mix making beating;
(5) slurries were dried 5-60 hour in 40-95 ℃ of water-bath, and dried 6-42 hour in 80-150 ℃ dry back again, then in 300-650 ℃ of following roasting 1-12 hour, and cooling, compression molding.
3. a kind of Fischer-Tropsch according to claim 1 synthesizes iron/manganese catalyst, it is characterized in that the atomic ratio of Fe in the catalyzer, Mn, Ca, K is: Fe: Mn: Ca: K=100: 5-30: 3-20: 1-5
SiO wherein
2Weight percent in catalyzer is 5-25wt%.
4. a kind of preparation method who is used for Fischer-Tropsch synthetic iron/manganese catalyst as claimed in claim 2, the concentration that it is characterized in that described mixing salt solution is the 0.10-1.00 mol.
5. a kind of preparation method who is used for Fischer-Tropsch synthetic iron/manganese catalyst as claimed in claim 2, the concentration that it is characterized in that described ammoniacal liquor is the 0.5-3.0 mol.
6. a kind of preparation method who is used for Fischer-Tropsch synthetic iron/manganese catalyst as claimed in claim 2 is characterized in that described temperature of reaction is 55-90 ℃, and the pH during reaction is 7.5-11.0.
7. a kind of preparation method who is used for Fischer-Tropsch synthetic iron/manganese catalyst as claimed in claim 2 is characterized in that SiO in the described catalyzer
2Content is 5-25wt%.
8. a kind of preparation method who is used for Fischer-Tropsch synthetic iron/manganese catalyst as claimed in claim 2 is characterized in that described solution of potassium carbonate concentration is the 0.1-1.0 mol.
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| CN 02121248 CN1203920C (en) | 2002-06-12 | 2002-06-12 | Ferromanganese catalyst for Fischer-Tropsch synthesis and method for preparing the same |
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|---|---|---|---|
| CN 02121248 CN1203920C (en) | 2002-06-12 | 2002-06-12 | Ferromanganese catalyst for Fischer-Tropsch synthesis and method for preparing the same |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1297343C (en) * | 2004-11-30 | 2007-01-31 | 中国科学院山西煤炭化学研究所 | Iron/manganese catalyst used for Fischer Tropsch synthesis, its preparation method and application |
| WO2009094936A1 (en) * | 2008-01-23 | 2009-08-06 | Accelergy Shanghai R & D Center Co., Ltd. | Catalyst for fischer-tropsch synthesis and its preparation method |
| WO2009100663A1 (en) * | 2008-01-23 | 2009-08-20 | Accelergy Shanghai R & D Center Co., Ltd. | Iron-based fischer-tropsch catalyst and method for making the same |
| WO2010121516A1 (en) * | 2009-04-22 | 2010-10-28 | 中科合成油技术有限公司 | Fischer–tropsch synthesis catalyst, preparation and application thereof |
| CN102076413A (en) * | 2008-06-24 | 2011-05-25 | 克斯莫石油株式会社 | Catalyst for fischer-tropsch synthesis, and process for production of hydrocarbon |
| CN102209699A (en) * | 2008-11-11 | 2011-10-05 | 吉坤日矿日石能源株式会社 | Method for manufacturing unsaturated hydrocarbon and oxygenated compound, catalyst, and manufacturing method therefor |
| CN102441384A (en) * | 2010-10-12 | 2012-05-09 | 中国石油化工股份有限公司 | Method for preparing low-carbon olefin catalyst by high-activity-stability carrier-type iron-based synthetic gas |
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| CN105688926A (en) * | 2014-11-24 | 2016-06-22 | 神华集团有限责任公司 | Fischer-tropsch iron-based catalyst high in low carbon olefin yield, and preparation method thereof |
| CN107617442A (en) * | 2016-07-15 | 2018-01-23 | 神华集团有限责任公司 | The method that F- T synthesis precipitated iron-based catalyst and its preparation method and application and synthesis gas synthesize hydrocarbon compound processed through syrup state bed Fischer Tropsch |
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2002
- 2002-06-12 CN CN 02121248 patent/CN1203920C/en not_active Expired - Lifetime
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| CN1297343C (en) * | 2004-11-30 | 2007-01-31 | 中国科学院山西煤炭化学研究所 | Iron/manganese catalyst used for Fischer Tropsch synthesis, its preparation method and application |
| WO2009094936A1 (en) * | 2008-01-23 | 2009-08-06 | Accelergy Shanghai R & D Center Co., Ltd. | Catalyst for fischer-tropsch synthesis and its preparation method |
| WO2009100663A1 (en) * | 2008-01-23 | 2009-08-20 | Accelergy Shanghai R & D Center Co., Ltd. | Iron-based fischer-tropsch catalyst and method for making the same |
| CN102076413B (en) * | 2008-06-24 | 2013-06-19 | 克斯莫石油株式会社 | Catalyst for fischer-tropsch synthesis, and process for production of hydrocarbon |
| CN102076413A (en) * | 2008-06-24 | 2011-05-25 | 克斯莫石油株式会社 | Catalyst for fischer-tropsch synthesis, and process for production of hydrocarbon |
| CN102209699A (en) * | 2008-11-11 | 2011-10-05 | 吉坤日矿日石能源株式会社 | Method for manufacturing unsaturated hydrocarbon and oxygenated compound, catalyst, and manufacturing method therefor |
| US8758596B2 (en) | 2008-12-26 | 2014-06-24 | Jx Nippon Oil & Energy Corporation | Hydrogenation isomerization catalyst, method for producing same, method for dewaxing hydrocarbon oil, and method for producing lubricant base oil |
| WO2010121516A1 (en) * | 2009-04-22 | 2010-10-28 | 中科合成油技术有限公司 | Fischer–tropsch synthesis catalyst, preparation and application thereof |
| RU2477654C1 (en) * | 2009-04-22 | 2013-03-20 | Синфьюэлс Чайна Текнолоджи Ко., Лтд | Fischer-tropsh synthesis catalyst, its production and application |
| CN102441384A (en) * | 2010-10-12 | 2012-05-09 | 中国石油化工股份有限公司 | Method for preparing low-carbon olefin catalyst by high-activity-stability carrier-type iron-based synthetic gas |
| CN105688926A (en) * | 2014-11-24 | 2016-06-22 | 神华集团有限责任公司 | Fischer-tropsch iron-based catalyst high in low carbon olefin yield, and preparation method thereof |
| CN105688926B (en) * | 2014-11-24 | 2020-08-21 | 国家能源投资集团有限责任公司 | Fischer-Tropsch iron-based catalyst for producing more low-carbon olefins and preparation method thereof |
| CN107617442A (en) * | 2016-07-15 | 2018-01-23 | 神华集团有限责任公司 | The method that F- T synthesis precipitated iron-based catalyst and its preparation method and application and synthesis gas synthesize hydrocarbon compound processed through syrup state bed Fischer Tropsch |
| CN107617442B (en) * | 2016-07-15 | 2020-07-14 | 神华集团有限责任公司 | Fischer-Tropsch synthesis precipitated iron-based catalyst, preparation method and application thereof, and method for preparing hydrocarbon compound by Fischer-Tropsch synthesis of synthesis gas through slurry bed |
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