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Fischer-Tropsch synthesis process applicable to fixed-bed reactor

A fixed-bed reactor, Fischer-Tropsch synthesis technology, applied in the petroleum industry, chemical instruments and methods, preparation of liquid hydrocarbon mixtures, etc. High efficiency, high selectivity and high heat transfer efficiency

Active Publication Date: 2014-04-02
中科潞安能源技术有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the existing process still cannot effectively remove the large amount of heat released by the Fischer-Tropsch reaction, and there is still the problem of catalyst bed overheating

Method used

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  • Fischer-Tropsch synthesis process applicable to fixed-bed reactor
  • Fischer-Tropsch synthesis process applicable to fixed-bed reactor
  • Fischer-Tropsch synthesis process applicable to fixed-bed reactor

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Experimental program
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Effect test

Embodiment 1

[0030] Prepare the catalyst Co / La / Ir / Al according to the method described in Chinese patent CN102962077A: Prepare a certain amount of 0.5mol / L sodium aluminate aqueous solution, drop 2ml of ammonia water, keep the temperature at 65°C, and keep the time for 60min, then press the sol Add peptizer HNO at a molar ratio of 0.1:1 to sodium aluminate 3 , stirred and refluxed until a transparent sol was maintained for 3 hours, and then aged at room temperature for 12 hours to obtain a gel. The gel was dried in a drying oven at 105°C for 6 hours, then the dry gel was placed in a temperature-programmed microwave oven at a heating rate of 2°C / min, and calcined at 350°C for 10 hours to obtain a catalyst carrier. Weigh Co(NO 3 ) 2 ·6H 2 O, LaCl 3 ·7H 2 O and IrCl 3 ·3H 2 O, measure deionized water according to the equal-volume impregnation method, prepare a mixed salt solution and impregnate the above-mentioned carrier for 5 hours, then dry at 100°C for 6 hours, and finally roast at...

Embodiment 2

[0035] Prepare catalyst Co / TiO by the method described in patent CN101269328 2 , dissolve 9.06g cobalt nitrate in 350ml butanol and stir well, add a certain amount of octadecylamine (molar ratio C 18 -NH 3 / Co=3), fully dissolved, then added 6.8ml of water, and finally added 24ml of butyl titanate, continued to stir for 24 hours, then dried by rotary evaporation under reduced pressure, dried at 100°C, and finally roasted at 500°C for 6h to obtain the catalyst. The weight composition is Co:TiO 2 =25.5:100, pressed into tablets and sieved for later use.

[0036] Take 100ml of the catalyst of 20-40 mesh and install it in a fixed bed reactor with an inner diameter of 14mm and a bed height of about 900mm. The upper 1 / 3 section of the bed is diluted with aluminum balls / catalyst (v / v)=1:2, the middle 1 / 3 section of the bed is diluted with aluminum balls / catalyst (v / v)=1:9, and the bottom 1 / 3 of the bed is diluted with aluminum balls / catalyst (v / v)=1:9 / 3 segments are not diluted....

Embodiment 3

[0040] The catalyst Co / Re / Si was prepared according to the method described in Chinese patent CN101269336. Using porous starch gel as a template, weighed 10g of potato starch and added it to 100g of water, heated to 90°C and stirred for 10min. Place in a refrigerator for 12 hours and then dry at room temperature for 24 hours to obtain a porous starch gel with a regular structure. Preparation solution TEOS:EtOH:NH 3 :H 2 O: Co: Re = 1: 30: 0.15: 0.45: 0.02, the solution was stirred at room temperature for 8 hours, and then impregnated into the pores of the starch template in three steps (starch gel / starch gel + solution = 20 (wt%) )). Immerse each step for 12 hours and dry at 120°C for 24 hours. Finally, it was baked at 550°C for 8 hours in an air atmosphere to remove the starch template, and a SiO containing 7.5wt% Co, 2wt% Re, 2 70.5wt% of the catalyst, pressed into tablets and sieved for later use.

[0041] Take 100ml of the catalyst of 20-40 mesh and install it in a fi...

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Abstract

The invention relates to a Fischer-Tropsch synthesis process applicable to a fixed-bed reactor. The process comprises the steps of dividing a bed layer into an upper section, a middle section and a lower section, loading a diluted catalyst, and enabling a circulating medium to enter the catalyst bed layer after the circulating medium is preheated; preheating raw material gas which is formed by mixing fresh synthesis gas and recycling gas, then enabling the preheated raw material gas to enter the catalyst bed layer for Fischer-Tropsch synthesis reaction, carrying out oil-gas-water three-phase separation on a reaction product, carrying out wastewater treatment on separated synthesis water, taking one part of the separated gas as purge gas, converging the other part of the separated gas and the fresh synthesis gas, and taking mixed gas as the raw material gas; separating the separated liquid, taking one part of C5-C8 obtained through separating as the circulating medium, and taking the rest of C5-C8 for other purposes. The process has the advantages of high heat exchange efficiency, 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 fixed-bed reactor. technical background [0002] Fischer-Tropsch synthesis of coal to produce fuel oil and chemicals is one of the important contents in the field of clean coal technology. Today, fluidized bed, slurry bed and fixed bed reactors are the main reactors for Fischer-Tropsch synthesis reactions. Although the fluidized bed reactor has high heat transfer coefficient and good heat transfer effect, it is easy to automate production, but its fluidization process is difficult to control, the catalyst utilization rate is low, back mixing, serious wear; although the slurry bed reactor has uniform reaction temperature, the production The efficiency is high, but there is also serious back mixing, and the separation of the catalyst is also a difficult problem to solve; the fixed bed reactor has the characteristics of uneven bed temperature distribution and poor bed thermal con...

Claims

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Application Information

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IPC IPC(8): C10G2/00B01J23/89
Inventor 李德宝李晋平侯博贾丽涛肖亚宁刘斌黄巍孙志强
Owner 中科潞安能源技术有限公司