Activating and starting method of fischer-tropsch synthetic catalyst

A technology for Fischer-Tropsch synthesis and Fischer-Tropsch synthesis of wax, which is applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc. It can solve the effects of catalyst activation, unstable wax product properties, and high driving costs. It can avoid the change of catalyst performance, keep the process conditions stable, and simplify the start-up operation of the device.

Active Publication Date: 2013-01-09
CHNA ENERGY INVESTMENT CORP LTD +1
View PDF4 Cites 2 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] This field usually adopts paraffin wax or liquid wax as the liquid phase medium used in the Fischer-Tropsch synthesis catalyst activation and start-up process, but finds that adopting paraffin wax or liquid wax as the liquid phase medium of catalyst activation has the following problems in many aspects through device operation experiments: The initial boiling point of paraffin or liquid wax is low. During the catalyst activation process, part of the liquid wax or paraffin is evaporated out of the activation reactor, resulting in a drop in the slurry level during the catalyst activation process. Paraffin or liquid wax needs to be supplemented to maintain the reactor liquid level; Since the temperature of external paraffin or liquid wax is lower than the activation temperature of the catalyst, it has a great influence on keeping the temperature of the reactor constant and affects the effect of catalyst activation; Fischer-Tropsch synthesis catalysts are very sensitive to sulfur, and the sulfur content of paraffin or liquid wax is required to be low If it is less than 0.5ppm, it is necessary to purchase specially processed paraffin or liquid wax. A large amount of liquid wax or paraffin is used during the start-up of the device, resulting in high start-up costs; due to the large difference in physical properties between paraffin wax or liquid wax and the Fischer-Tropsch synthetic wax generated by the reaction, Before replacing most of the paraffin or liquid wax out of the reactor, the properties of the wax product extracted from the reactor have been unstable, and the device is also in an unstable state, resulting in more difficulties in the operation of the device during the start-up process
[0004] In addition, when the activated Fischer-Tropsch synthesis catalyst is transported to the Fischer-Tropsch synthesis unit for the Fischer-Tropsch synthesis reaction, a slurry pump is generally used to transport the slurry containing the catalyst, which causes catalyst wear, reduces catalyst life, and increases the iron content of the Fischer-Tropsch synthesis product. Detrimental to the long-term operation of the device
[0005] In summary, the prior art has not yet disclosed a method for activating and starting the Fischer-Tropsch synthesis catalyst that can effectively solve the above problems

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0039] The Fischer-Tropsch synthesis unit used in the test is an industrial demonstration of 180,000 tons / year. After the device has been shut down for maintenance, it should be restarted according to the following steps:

[0040] First, the catalysts were activated using Fischer-Tropsch waxes as shown in Table 1. In the process of Fischer-Tropsch synthesis catalyst activation, Fischer-Tropsch synthesis wax is injected into the Fischer-Tropsch activation reactor, and then it is preheated to 150°C, and the pre-mixed Fischer-Tropsch synthesis wax and catalyst are input into the activation reactor. Slurry, then control the liquid level of the activation reactor at 20m by supplementing Fischer-Tropsch wax, adjust the pressure and superficial gas velocity of the activation system to the required value (Table 2) and raise the temperature to 260°C, and the activation time is 24 hours. During the constant temperature period, the Fischer-Tropsch synthetic wax is supplemented as needed...

Embodiment 2

[0048] The Fischer-Tropsch synthesis unit used in the test is an industrial demonstration of 180,000 tons / year. After the device has been shut down for maintenance, it should be restarted according to the following steps:

[0049] First, the Fischer-Tropsch synthesis wax as shown in Table 3 is used for catalyst activation. In the process of Fischer-Tropsch synthesis catalyst activation, the Fischer-Tropsch synthesis wax is injected into the activation reactor, which is preheated to 150 ° C, and then activated. Input the mixed slurry of Fischer-Tropsch synthetic wax and catalyst mixed in advance in the reactor, then control the liquid level of the activation reactor at 20m by supplementing Fischer-Tropsch wax, adjust the pressure of the activation system and the superficial gas velocity to the required value (Table 4) And raise the temperature to 255°C, and the activation time is 24 hours. During the constant temperature period, the Fischer-Tropsch synthetic wax is supplemente...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
melting pointaaaaaaaaaa
Login to view more

Abstract

An activating and starting method of a fischer-tropsch synthetic catalyst comprises the following steps of (1) adding the catalyst in an activation reactor to activate partial needed fischer-tropsch synthetic wax and preheating to 100-180 DEG C; (2) injecting mixed slurry of the pre-mixed fischer-tropsch synthetic wax and the catalyst in the activation reactor, supplementing the fischer-tropsch synthetic wax to enable the formed mixed slurry to achieve a preset liquid level in the activation reactor, and evenly mixing the fischer-tropsch synthetic wax and the catalyst to be activated; (3) conducting catalyst activation at needed activation conditions; and (4) transporting activated catalyst slurry to a fischer-tropsch synthetic reactor to be used for conducting a fischer-tropsch synthetic reaction. By means of the method, starting cost can be obviously reduced, and buying of a large quantity of paraffin wax and liquid wax is avoided.

Description

technical field [0001] The invention relates to a Fischer-Tropsch synthesis process, more specifically, a method for activating and starting a Fischer-Tropsch synthesis catalyst. Background technique [0002] In the Fischer-Tropsch synthesis reaction process using the slurry bed as the synthesis reactor, since the Fischer-Tropsch synthesis catalyst produced is in an oxidized state, the active phase of the Fischer-Tropsch synthesis reaction is Fe x C. The catalyst needs to be activated before the reaction, so that the catalyst can obtain a stable active phase for the Fischer-Tropsch synthesis reaction. Before the operation of the device, a certain amount of liquid phase medium (slurry bed is three phases) needs to be pre-added in the activation reactor and the synthesis reactor, so that the catalyst is activated in the activation reactor and then transferred to the synthesis reactor. react. [0003] This field usually adopts paraffin wax or liquid wax as the liquid phase me...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C10G2/00B01J37/04
Inventor 周从文徐志新马芳伟张杰贺飞王欣
Owner CHNA ENERGY INVESTMENT CORP LTD
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products