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Method for inhibiting hydrocarbons steam cracking furnace from coking and carburizing

A cracking furnace and steam technology, used in cracking, non-catalytic thermal cracking, petroleum industry, etc., can solve the problems of difficult maintenance, influence of downstream systems, long time for injecting inhibitors, etc. Thermal effect, effect of suppressing catalytic coking

Active Publication Date: 2012-05-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Disclosed in CN1236827A is a method for suppressing and slowing down the coke formation and deposition in the pyrolysis of hydrocarbons, using one or more mixtures of hydrogen sulfide, organosulfur compounds, organophosphorus compounds and organosulfur phosphorus compounds to carry out thermal cracking equipment Pretreatment, but the effect of inhibiting coking is not very ideal
Carburizing causes the furnace tube to creep and rupture, which greatly shortens the service life of the furnace tube
[0009] The existing coking suppression methods in the prior art have the following disadvantages: 1) It affects the downstream system, making the operation of the latter system difficult; 2) The additive is toxic and pollutes the environment; 3) The inhibitor is injected before the cracking furnace is put into oil. If the time is too long, the ethylene output will be reduced; 4) processing and maintenance are difficult and the cost is high; 5) the carburization of the cracking furnace tube cannot be effectively improved; 6) the effect of inhibiting coking and carburization is not ideal, etc.
[0011] However, only setting enhanced heat transfer furnace tubes such as twisted sheet tubes in the radiant section of the ethylene cracking furnace has limitations. The operating cycle of the furnace, but there is still coking between the enhanced heat transfer components such as twisted sheets and the inner wall of the furnace tube. After a period of operation, the cracking furnace will have to be shut down due to severe coking

Method used

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  • Method for inhibiting hydrocarbons steam cracking furnace from coking and carburizing
  • Method for inhibiting hydrocarbons steam cracking furnace from coking and carburizing
  • Method for inhibiting hydrocarbons steam cracking furnace from coking and carburizing

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] Embodiment 1 and embodiment 2 are the result that industrial cracking furnace is processed.

[0047] Example 1

[0048] Set the solid content to 20%, SiO 2 / Al 2 o 3 =8, PH is that the aluminum silicate sol of 3~4 is diluted with water to be the SiO that oxide mass concentration is 1% 2 —Al 2 o 3 Aqueous solution of sol. The device is a 60,000 tons / year ethylene SRT-IV (HC) industrial cracking furnace, which is divided into six groups of feed materials, and three waste heat boilers are connected in parallel, and are arranged in the form of mutual intervals in the furnace tube of the cracking furnace radiant section along the axial direction The twisted sheet tube made integrally with the furnace tube, the twisted sheet is twisted 180°, and the distance between two adjacent twisted sheets is 15 pitches; during the hot standby after the cracking furnace is burnt, the outlet temperature of the cracking furnace is 700 ~850°C, under the operating pressure of 0.4Mpa,...

Embodiment 2

[0050] Set the solid content to 20%, SiO 2 / Al 2 o 3 =8, PH is that the aluminum silicate sol of 3~4 is diluted with water to be the SiO that oxide mass concentration is 2% 2 —Al 2 o 3 Aqueous solution of sol. The device is a 30,000-ton / year ethylene GK-V cracking furnace, which is divided into four groups of feed materials. There are two waste heat boilers. In the furnace tube of the radiant section of the cracking furnace, twisted sheet tubes are arranged in the form of mutual intervals, and the twisted sheets are twisted. 180°, the distance between two adjacent twisted sheets is 20 pitches; during the hot standby period after the cracking furnace is burnt, the outlet temperature of the cracking furnace is 700-850°C, and under the operating pressure of 0.3Mpa, the diluted Good SiO 2 —Al 2 o 3 The sol aqueous solution is injected from the spanning section of the cracking furnace accompanied by carrier gas water vapor (10kg / h), wherein SiO 2 / Al 2 o 3 The molar rati...

Embodiment 3

[0055] Simulate the SRT-III type cracking furnace, adopt the method of the present invention, add 3 sections of twisted sheet tubes in the furnace tube of the radiant section, and when the outlet temperature of the cracking furnace is 800 ° C, SiO 2 Neutral silica sol with a mass concentration of 20% and a pH of 6.5 to 7.5 is diluted with water to SiO with a mass concentration of 0.5% pure oxide 2 Aqueous sol solution is injected from the spanning section of the cracking furnace, the injection amount is 200g / h, and the injection time is 1 hour, SiO 2 The sol forms a layer of ceramic film on the inner wall of the cracking furnace tube, which can inhibit the coking and carburizing of the furnace tube. After using the above method to treat the cracking furnace tube, use naphtha as raw material for steam cracking, its physical properties are: distillation range 48-211°C, specific gravity D 15.6 0.7287g / ml, sulfur content 165PPM; cracking conditions: cracking temperature 840°C, re...

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Abstract

The invention relates to a method for suppressing coking and carburizing of hydrocarbon steam cracking furnaces, which comprises the following steps: arranging at least one segment of heat transfer enhancement furnace pipe in the furnace pipe of radiation section of the cracking furnace, and preprocessing the hydrocarbon steam cracking furnace by using a sol composition during heat reserve periodof the cracking furnace, wherein the sol composition contains at least one selected from Si sol, Al sol and Zr sol, and the mass concentration of pure oxide in the sol composition is 0.1 to 10% the weight of the sol composition. The method provided by the invention has the advantages of low cost, simple operation, environment friendliness, and no influence on downstream system, and can significantly prolong the service life and the operation cycle of the cracking furnace on the basis of effectively suppressing coking and carburizing of the cracking furnace pipe, thus improving output of ethylene products, etc. and improving the economic benefit of an ethylene plant.

Description

technical field [0001] The invention relates to a method for suppressing coking and carburization of hydrocarbon steam cracking furnaces in the field of petrochemical industry. Background technique [0002] In the pyrolysis ethylene production plant, the cracking furnace is the most critical core equipment, and about 60% of the energy consumption of ethylene production is consumed in the cracking furnace. The cracking furnace tube is the component with the highest operating temperature in the ethylene production device. The cracking reaction of hydrocarbons is carried out in the furnace tube. Due to the secondary reactions such as polymerization and condensation, it is inevitable to generate coke on the inner wall of the cracking furnace tube and the inner wall of the quenching boiler tube. dirt. Coking increases the thermal resistance of the tube wall, reduces the heat transfer coefficient, increases the wall temperature and causes local overheating; coking increases the e...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G9/16C10G9/20C10G9/36
Inventor 王红霞王国清陈硕戴伟张利军
Owner CHINA PETROLEUM & CHEM CORP
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