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Method for utilizing Fischer-Tropsch synthesis product

A Fischer-Tropsch synthesis and product technology, which is applied in the petroleum industry, hydroprocessing process, and hydrocarbon oil treatment, etc., can solve the problems of insufficient utilization of Fischer-Tropsch synthesis products, single economic benefits of production line products, and low raw material utilization, etc., to achieve rich The effect of product content, the ability to achieve refined utilization, and the ability to increase price fluctuations

Inactive Publication Date: 2020-06-05
CHINA ENERGY GRP NINGXIA COAL IND CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the above method, the utilization of Fischer-Tropsch synthesis products is not fine enough, and other valuable components in Fischer-Tropsch synthesis products, such as α-olefins, are not fully utilized, which not only increases the processing load of the device, but also causes a waste of resources
[0006] It can be seen from the above that there are many problems in the method for producing candle raw materials in the prior art, such as single production line products, low economic benefits, or waste of resources caused by insufficient raw material utilization.

Method used

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  • Method for utilizing Fischer-Tropsch synthesis product
  • Method for utilizing Fischer-Tropsch synthesis product
  • Method for utilizing Fischer-Tropsch synthesis product

Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach

[0036] According to a preferred embodiment of the present invention, the first distillation obtains a wax oil fraction with a distillation range greater than 450°C. Under this preferred embodiment, the production cost is further reduced, and it is more conducive to the refined utilization of Fischer-Tropsch synthesis products.

[0037] According to the present invention, the hydrofinishing adopts the method of catalytic hydrogenation to remove unsaturated olefins, aromatics and oxygen-containing compounds in the wax oil fraction, and to produce candle raw materials and high melting point waxes with the obtained Fischer-Tropsch synthesis refined wax, which solves the problem of The problem that the color number of the product is too low is caused by the coking of the material in the subsequent distillation and separation process.

[0038] In the present invention, the range of conditions for hydrofinishing the wax oil fraction is relatively wide, and in a specific embodiment, t...

specific Embodiment approach

[0044] In the present invention, the second distillation can be carried out by using multiple distillation towers connected in series, or by using a single distillation tower under reduced pressure and elevated temperature conditions. In the present invention, the distillation tower for the second distillation is not particularly limited, specifically, it may be a short-path distillation device, a vacuum still distillation apparatus, or a rectification tower. The short-path distillation device is a system that uses the free path of material molecules to divide raw materials into products of different fractions. In a specific embodiment, the rectification column is a sieve tray column.

[0045] In the present invention, the selection range of the second distillation of the Fischer-Tropsch synthesis refined wax obtained by the hydrofinishing is relatively wide.

[0046] Preferably, the distillation conditions of the fraction 1 include: a pressure of 0.5-1.5kPa and a temperature...

Embodiment 1

[0090] The utilization method of the Fischer-Tropsch synthesis product in this embodiment adopts figure 1 In the process flow shown, the raw material used is the Fischer-Tropsch synthesis product from the oil synthesis unit of the 4 million tons / year coal-to-oil branch of Guoneng Ningxia Coal Industry Company. The properties are listed in Table 1.

[0091] The active component of the catalyst used in hydrofining reactor 2 is MoO 3 / NiO, as oxide, MoO 3 The weight ratio to NiO is about 2:5, and the support is Al 2 o 3 , based on the dry basis weight of the catalyst, the content of the active component is 12% by weight, the catalyst is in the shape of a four-leaf clover, and its bulk density is 0.57g / cm 3 about. The operating pressure of the reactor is 7MPa, the temperature is 270°C, and the liquid hourly volume space velocity is 2h -1 , The volume ratio of hydrogen to oil is 350:1.

[0092] Table 1

[0093]

[0094]

[0095] Send the above-mentioned Fischer-Tropsch...

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Abstract

The invention relates to the field of Fischer-Tropsch synthesis product utilization, and discloses a Fischer-Tropsch synthesis product utilization method, which comprises: (1) carrying out first distillation on a Fischer-Tropsch synthesis product to obtain a wax oil fraction with a distillation range of more than 400 DEG C; (2) carrying out hydrofining on the wax oil fraction to obtain Fischer-Tropsch synthesis refined wax; (3) carrying out second distillation on the Fischer-Tropsch synthesis refined wax to obtain a fraction 1 and a fraction 2; and (4) mixing the fraction 1 and the fraction 2according to a weight ratio of 0.1-10: 1 to obtain a candle raw material. According to the method disclosed by the invention, the energy consumption of the equipment is reduced, meanwhile, the co-production of the Fischer-Tropsch synthesis candle raw material, a high-melting-point wax and the C5 and above narrow fraction section fractions is achieved, and the fine utilization of the Fischer-Tropsch synthesis product is realized.

Description

technical field [0001] The invention relates to the utilization field of Fischer-Tropsch synthesis products, in particular to a utilization method of Fischer-Tropsch synthesis products. Background technique [0002] Wax is a mixture of n-alkanes that is solid at room temperature and is widely used in inks, explosives, plates, candles and other products. At present, most waxes on the market are prepared through traditional petroleum refining methods. Due to the complexity of the composition of traditional petroleum itself and the limitations of its preparation process, there are often sulfur, nitrogen, and aromatic compounds in the candles and high-melting point wax products produced. The environment produces pollution. [0003] With the country's increasing emphasis on environmental protection and the increasingly stringent environmental laws and regulations, the raw materials of wax are required to develop in the direction of low pollution and green environmental protecti...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G67/02
CPCC10G67/02C10G2300/1022C10G2300/301
Inventor 邵光涛刘素丽张安贵金政伟袁华安良成梁雪美
Owner CHINA ENERGY GRP NINGXIA COAL IND CO LTD