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Slurry bed reaction system and method for Fischer-Tropsch synthesis reaction

A reaction system, Fischer-Tropsch synthesis technology, applied in chemical instruments and methods, preparation of liquid hydrocarbon mixtures, chemical/physical processes, etc., can solve problems such as increased proportion, test failure, complex manufacturing, etc., to improve heat exchange efficiency , improve safety and ensure the effect of yield

Active Publication Date: 2020-11-27
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0011] However, this kind of pin-fin heat exchanger has the characteristics of complicated manufacturing, and with the increase of the size of the reactor, it is necessary to increase the length and number of pin-fins on the tubes, which increases the heat transfer effect under the premise of ensuring the heat exchange effect. Manufacturing is difficult, and at the same time, the proportion of the cross-sectional area of ​​the heat exchange tubes to the cross-sectional area of ​​the reactor increases, which affects the fluid distribution inside the reactor and will lead to a decrease in the yield of the target product
[0012] In addition, the Fischer-Tropsch reaction is a strong exothermic reaction. Once the Fischer-Tropsch synthesis reactor has overheating, the heat exchanger has no measures to remove the excess heat in time, which will cause the test to fail in severe cases.

Method used

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  • Slurry bed reaction system and method for Fischer-Tropsch synthesis reaction
  • Slurry bed reaction system and method for Fischer-Tropsch synthesis reaction
  • Slurry bed reaction system and method for Fischer-Tropsch synthesis reaction

Examples

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Embodiment approach

[0039] According to a preferred embodiment of the present invention, 20-70% of the heat exchange tubes of the internal heat exchange unit are provided with baffles.

[0040] According to a preferred embodiment of the present invention, the internal heat exchange unit includes a lower heat exchange unit 2, a middle heat exchange unit 3 and an upper heat exchange unit 4 arranged inside the slurry bed reactor 1;

[0041] The lower heat exchange unit 2, the middle heat exchange unit 3 and the upper heat exchange unit 4 each include a plurality of parallel heat exchange tubes, and part or all of the lower heat exchange unit 2 and the middle heat exchange unit 3 Baffles are respectively arranged in the heat exchange tubes, and the baffles are used to prolong the residence time of the heat exchange medium in the internal heat exchange unit;

[0042] Relative to the heater (6), the lower heat exchange unit 2, the middle heat exchange unit 3 and the upper heat exchange unit 4 are conne...

Embodiment 1

[0098] This example is used to illustrate the slurry bed reaction system and the Fischer-Tropsch synthesis reaction method of the present invention.

[0099] use figure 1 In the slurry bed reaction system shown, the Fischer-Tropsch synthesis feed gas (synthesis gas) is introduced from the lower part of the slurry bed reactor 1, and then reacts on the surface of the catalyst in the environment of liquid wax, and the gas produced after the reaction is released from the reactor The top flows out to the downstream for separation, and the heater 6 makes the temperature rise rate of the flowing water 20°C / h; when the temperature in the slurry bed reactor 1 reaches 120°C, the heater 6 is set so that the temperature rise rate of the flowing water 10°C / h; when the temperature in the slurry bed reactor 1 reaches 200°C, set the heater 6 so that the temperature rise rate of the water flowing through it is 5°C / h; when the temperature in the slurry bed reactor 1 reaches 250°C , it is consi...

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Abstract

The invention relates to the field of Fischer-Tropsch synthesis, and particularly provides a slurry bed reaction system and a method. The slurry bed reaction system comprises a slurry bed reactor, aninternal heat exchange unit and an external heat exchange unit, wherein the external heat exchange unit comprises a steam drum and a heater, the steam drum and the heater are sequentially connected inseries, the heater is communicated to the lower-portion water inlet of the internal heat exchange unit, the steam drum is communicated to the upper-portion water outlet of the internal heat exchangeunit, the internal heat exchange unit comprises heat exchange pipes, and baffles are arranged inside the part of or all of the heat exchange pipes, and are used for prolonging the residence time of aheat exchange medium in the internal heat exchange unit. With system of the present invention, the heat exchange efficiency of the heat exchange unit in the reactor can be improved, the uniform and stable temperature inside the slurry bed reactor can be ensured, and the excess heat caused by the temperature runaway can be effectively removed when the catalyst is subjected to local temperature runaway so as to ensure the yield of the target product and improve the operation safety of the device.

Description

technical field [0001] The invention relates to the field of Fischer-Tropsch synthesis, in particular to a slurry bed reaction system and a method for Fischer-Tropsch synthesis. Background technique [0002] With the continuous rise of oil prices in recent years, people pay more and more attention to the development of technologies to produce alternative oil products. Syngas is produced through coal, natural gas or other substances, and then according to the requirements of the Fischer-Tropsch synthesis catalyst for synthesis gas, through water-gas shift and synthesis The gas purification process processes the syngas, and uses the treated syngas as a raw material to produce hydrocarbons through Fischer-Tropsch synthesis, and at the same time produces oxygenated compounds, which are then processed by mature petroleum processing technology to produce high-quality, environmentally friendly oil. Taste. The development of Fischer-Tropsch synthesis technology is of great signific...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/22C10G2/00
CPCB01J8/22B01J2208/00106C10G2/32C10G2/34
Inventor 杜冰卜亿峰刘潇姚德良苗强胡云剑孙永伟
Owner CHNA ENERGY INVESTMENT CORP LTD
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