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A Fischer-Tropsch synthesis process suitable for trickle bed reactor

A technology of Fischer-Tropsch synthesis and reactors, which is applied in the petroleum industry and the preparation of liquid hydrocarbon mixtures, etc. It can solve the problems of low effective utilization of reactor space, difficulty in controlling the supercritical state, and poor wetting rate of process catalysts. , achieve the effect of high target product yield, high production capacity, and avoid overheating

Active Publication Date: 2016-01-27
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In order to solve the heat transfer problem of the fixed bed Fischer-Tropsch reaction, C.O.Vandu (Hydrodynamics and mass transfer inan upflow monolith loop reactor, Chemical Engineering and Processing, 44, 2005, 363–374) (Vandu La, liquid dynamics and mass transfer in monolithic reactor with medium upflow, Chemical Engineering and Technology, 44, 2005, 363-374) The monolithic catalyst is applied to the Fischer-Tropsch synthesis process of oil circulation, which has a certain heat transfer effect, but there are problems such as large oil circulation power consumption, large pressure drop of the reactor, and Problems such as low effective utilization of space
Xiwen Huang (Selective Fischer–Tropsch synthesis overan Al 2 o 3 supported cobaltcatalystinsupercriticalhexane, Fuel Processing Technology, 83, 1-3, 2003, 81–99) ) using supercritical spray n-hexane process for Fischer-Tropsch synthesis reaction, and obtained some meaningful results, but the catalyst wetting rate of this process is not good, and it is difficult to grasp the supercritical state, so it is not suitable for industrial production
ByH.E.Benson (development of the fischer-tropschoil-recycle process, bulletin 568, united states government printing office, Washington: 1957) The synthesis process is applied to the expanded bed reactor with high production capacity and difficult temperature control, and a good bed temperature curve distribution has been obtained. The oil circulation Fischer-Tropsch synthesis process is used in the trickle bed reactor, and no report has been found after searching

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  • A Fischer-Tropsch synthesis process suitable for trickle bed reactor
  • A Fischer-Tropsch synthesis process suitable for trickle bed reactor
  • A Fischer-Tropsch synthesis process suitable for trickle bed reactor

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Embodiment 1

[0029] Prepare catalyst by the method described in patent CN1463794: take Fe(NO 3 ) 3 9H 2 O194.07g, Ca(NO 3 ) 2 4H 2 Og and 50% Mn(NO 3 ) 2 85.99 g of the solution was prepared with deionized water to form a mixed solution with a total concentration of 0.3 mol / L, and the mixed solution was heated in a water bath at 50°C; the ammonia solution with a concentration of 0.5mol / L was prepared and heated in a water bath at 50°C; Slowly add the above ammonia solution into the salt solution, stir, and the precipitation process takes about 35 minutes. When the precipitation ends, the pH=8.5, let it stand for 12 hours, and filter with suction. The filter cake is washed with deionized water until pH=7.5, and then filtered with suction. Dry at 110-120°C for 24 hours; grind the dried filter cake finely, impregnate with 16ml of potassium carbonate with a concentration of 0.91mol / L for 3 hours, dry at 75°C; then roast at 500°C for 5 hours, and press at 50MPa to tablet. The atomic rati...

Embodiment 2

[0032] The catalyst is prepared according to the method described in the patent CN101269336: the porous carbon material is used as a template, and the biomass material corn is used as a carbon source, and it is processed in a microwave oven for 3 minutes to obtain popcorn with good expansion. The treated popcorn was placed in a high-temperature tube furnace and carbonized at 900°C for 4 hours in a nitrogen atmosphere. A carbon template with a honeycomb macroporous structure and a uniform microporous structure is obtained. Preparation solution TEOS:EtOH:NH 3 : H2O=1:30:0.15:2, the solution was stirred at room temperature for 6h, and then impregnated into the pores of porous carbon in three steps (porous carbon / porous carbon+solution=30(wt)%). Immerse each step for 24 hours and dry at 100°C for 24 hours. Finally, it was calcined at 600° C. under an air atmosphere for 6 hours to remove the carbon template to obtain a hierarchically porous silica carrier. Weigh 9.3gCo(NO 3 ) ...

Embodiment 3

[0035] Prepare catalyst 30%Co / SiO by the method described in patent CN101269329 2 , weighed 7.4 grams of cobalt nitrate hexahydrate, dissolved in 20 mL of deionized water to obtain a uniform solution, and used commercial silica gel as a carrier (specific surface area 176m 2 / g, average pore diameter 11.32nm), impregnated by ordinary impregnation method, left at room temperature for 24h, dried in a vacuum oven at 60°C for 24h, after the dried solid was fully ground, baked in air at 500°C for 10h, and roasted The solid powder was slowly heated to 300°C for 10 hours for reduction treatment in a hydrogen atmosphere, and then cooled naturally. After cooling down to room temperature, it was switched to CO passivation gas for passivation for 10 hours, and it was pressed into tablets for use.

[0036] Take 300ml of the catalyst of 20-40 mesh and put it in a trickle bed reactor, the inner diameter of the reactor is 35mm, the height of the reactor is 500mm, and the effective bed height ...

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Abstract

The invention discloses a Fischer-Tropsch synthesis process applicable to a trickle bed reactor, which comprises the following steps: a fresh synthesis gas and a circulating medium are mixed and enter the trickle bed reactor from a feed port; the mixture sequentially passes through a gas-liquid distributor and a porcelain ball bed layer and enters a catalyst bed layer to perform a Fischer-Tropsch synthesis reaction; the products are gathered and subjected to oil-gas-water three-phase separation; the separated synthetic water is subjected to wastewater treatment; the separated gas enters a circulating buffer tank; when in a stable state, one part of the gas is discharged as purge gas, and the rest part of the gas is mixed with fresh synthesis gas as a circulating gas, and the mixture is used as a feed gas which enters the reactor again; the separated liquid enters a rectifying tower for rectification; and one part of the liquid fraction obtained by rectifying separation is used as a circulating medium which flows into the trickle bed reactor together with the feed gas. The Fischer-Tropsch synthesis process disclosed by the invention has the advantages of large capacity, uniform bed layer temperature, stability in operation and easiness in control.

Description

technical field [0001] The invention relates to a Fischer-Tropsch synthesis process suitable for a trickle bed reactor. technical background [0002] The clean utilization of coal is the theme of the current energy field, and the preparation of fuel oil and chemicals by coal-based Fischer-Tropsch synthesis is one of the important contents in the field of clean coal technology. Fixed bed, fluidized bed and slurry bed reactors are the main reactors for Fischer-Tropsch synthesis. The fluidization process of the fluidized bed reactor is difficult to control, the utilization rate of the catalyst is low, back mixing, and serious wear; the fixed bed reactor has the disadvantages of small catalyst loading and poor thermal conductivity of the bed, which makes the capacity of the fixed bed reactor small, And it is easy to overheat, which limits industrial application; although the slurry bed reactor has been applied in industry, it also has serious back-mixing. Although the iron-base...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G2/00
Inventor 李德宝刘岩侯博贾丽涛陈从标王俊刚
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI