Technology and device for producing national standard oil through fischer-tropsch synthesis oil and coal tar through hydrogenation

A technology for Fischer-Tropsch synthetic oil and coal tar, applied in the field of coal chemical industry, can solve the problems of low single-pass conversion rate, low diesel yield, small profit margin, etc., and achieve high one-pass conversion rate, low operating cost, and good product quality. Effect

Inactive Publication Date: 2015-10-21
SHAANXI MEISILIN ENERGY SCI & TECH RES INST
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

It also cannot enter the official sales channel of finished products in my country, and can only be used as a blending component of refined oil, which has the disadvantages of low market price and small profit margin
[0004] However, the current Fischer-Tropsch synthetic oil hydroprocessing unit and tar hydrogenation lightening unit adopt the traditional petroleum refining hydrogenation process, which is not specific to the composition characteristics of Fischer-Tropsch synthetic oil and coal tar, resulting in production failures. Diesel oil cannot fully meet the standard (GB1947-2013 IV), the single-pass conversion rate is low, the yield of diesel oil is low, and the heavy distillate oil in the reaction oil is repeatedly circulated, which eventually causes the system resistance to rise rapidly, and the continuous operation cycle is often only about 7000 hours
Moreover, during the hydrogenation reaction of coal tar, the heavy asphaltenes that have not completely reacted are precipitated in the form of colloids during the cooling process, adhering to the inner surface of the pipeline and heat exchange equipment, causing a large drop in pipeline resistance, poor heat exchange equipment, and even causing Failure of key instruments in the hydrogenation process unit directly threatens the safe and stable operation of the hydrogenation process unit

Method used

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  • Technology and device for producing national standard oil through fischer-tropsch synthesis oil and coal tar through hydrogenation
  • Technology and device for producing national standard oil through fischer-tropsch synthesis oil and coal tar through hydrogenation
  • Technology and device for producing national standard oil through fischer-tropsch synthesis oil and coal tar through hydrogenation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] Fully mix Fischer-Tropsch synthetic oil (low temperature fee) at 70-80°C and coal tar (medium-low temperature or high temperature) at 80-85°C in a mixing tank at a ratio of 0.1-10. The mixing tank is pressurized with hydrogen to 0.8-2.5MPa (gauge pressure) for isolation and sealing. The mixed mixed oil is used as hydrogenation raw material oil, and enters the raw material oil heater through the bottom of the mixing tank to exchange heat with 300°C heat transfer oil to 230-260 After ℃, pressurize to 15.2-19.1MPa (gauge pressure) by the raw oil pump. The pressurized raw material oil and the mixed hydrogen from the high-pressure heat exchanger after heat exchange and temperature rise are mixed in the pipeline and enter the start-up heating furnace. The volume ratio of hydrogen and raw oil is 550-800. During normal operation, the starting heating furnace is in a stuffy state, and the temperature of the raw material oil does not change. The raw material oil from the start-u...

Embodiment 2

[0054] Fully mix Fischer-Tropsch synthetic oil (low-temperature Fischer-Tropsch synthetic oil) a at 72°C and coal tar (medium-low temperature coal tar) b at 81°C at a ratio of 0.35 in the mixing tank 1, and the mixing tank 1 is pressurized with hydrogen to 1.1MPa (gauge pressure) for isolation and sealing. The mixed mixed oil is used as hydrogenation raw material oil, and enters the raw material oil heater 2 through the bottom of the mixing tank 1 to exchange heat with the 300°C heat transfer oil to 243°C, and then the raw oil pump 3 is used for hydrogenation. Pressure to 16.2MPa (gauge pressure). After the pressurization, the raw material oil and mixed hydrogen are mixed in the pipeline and enter the start-up heating furnace 4, and the volume ratio of the hydrogen gas and the raw material oil is 610. During normal operation, the start-up heating furnace 4 is in a stuffy state, and the temperature of the raw material oil does not change. The raw material oil coming out from t...

Embodiment 3

[0056] The Fischer-Tropsch synthetic oil (low-temperature fee) a of 74 ° C and the coal tar (high-temperature coal tar) b of 85 ° C are fully mixed in the mixing tank 1 at a ratio of 2.1, and the mixing tank 1 is pressurized to 1.46 MPa ( Gauge pressure) for isolation and sealing, the mixed mixed oil is used as the hydrogenation raw material oil, enters the raw material oil heater 2 through the bottom of the mixing tank 1, exchanges heat with the 300°C heat transfer oil to 253°C, and then is pressurized to 17.6MPa by the raw oil pump 3 (Gauge). After the pressurization, the raw material oil and the mixed hydrogen are mixed in the pipeline and enter into the start-up heating furnace 4, and the volume ratio of hydrogen to oil is 721. During normal operation, the start-up heating furnace 4 is in a stuffy state, and the temperature of the raw material oil does not change. The raw material oil coming out from the start-up heating furnace 4 enters the lightening reactor 5 . The op...

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Abstract

The invention discloses a technology and device for producing national standard oil through fischer-tropsch synthesis oil and coal tar through hydrogenation. The device comprises a mixed raw oil supply device, a start heating furnace, a reactor and a high-pressure heat exchanger. An outlet of the mixed raw oil supply device is connected with a raw material inlet of the start heating furnace, an outlet of the start heating furnace is connected with an inlet of the reactor, a gas phase outlet of the reactor is connected with an inlet of the high-pressure heat exchanger, hydrogen is introduced into another inlet of the high-pressure heat exchanger, one outlet of the high-pressure heat exchanger is connected with a cooling separation device through a pipeline with a desalted water inlet, another outlet of the high-pressure heat exchanger is connected with the raw material inlet of the start heating furnace, and a liquid phase outlet of the reactor discharges separated product oil. The technology and device for producing the national standard oil through the fischer-tropsch synthesis oil and the coal tar through hydrogenation have the advantages that the conversion rate per pass is high, the technological process is short, the number of high-pressure devices is small, investment cost is reduced, operation cost is low, product quality is good, and safety and reliability are achieved.

Description

technical field [0001] The invention belongs to the field of coal chemical industry, and in particular relates to a process and a device for co-hydrogenating Fischer-Tropsch synthetic oil and coal tar to produce national standard oil. Background technique [0002] With the rapid development of my country's national economy, the demand for refined oil is increasing, and the income of Chinese residents is growing steadily, and the living standard is constantly improving, making the consumption of refined oil still in a stage of rapid growth. However, my country's oil resources are in short supply. It has become an important restrictive factor for my country's economic development. In order to ensure national energy security and sustainable economic development, my country's coal-to-oil products have developed rapidly in the past decade. In addition, my country's urban air pollution is developing from coal-burning emissions to motor vehicle emissions and compound pollution. In...

Claims

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Application Information

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IPC IPC(8): C10G67/02
Inventor 佘焱董芳儒
Owner SHAANXI MEISILIN ENERGY SCI & TECH RES INST
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