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Complex catalyst for viscosity reduction of thick oil by hydrothermal catalytic cracking and preparation and application thereof

A catalyst and thermal catalysis technology, applied in catalytic cracking, organic compound/hydride/coordination complex catalysts, physical/chemical process catalysts, etc., can solve problems such as ineffective field application, poor contact with crude oil, and high operating temperature. Achieve the effect of simple production, reduce viscosity and improve the quality of heavy oil

Active Publication Date: 2012-05-30
PETROCHINA CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

These viscosity reducers have the disadvantages of high use temperature, poor universality, poor contact with crude oil, and high concentration, so it is difficult to be effective in field application

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] 5gC 12 The carboxylic acid was mixed with 2.0 g of ethylenediamine and the oil bath was heated to 180°C for 2h. The temperature was lowered to 90°C, and an aqueous solution containing 9.5 g of sodium chloroacetate was added. After stirring for 40 minutes, 3.8g of NaOH was added, and the reaction was continued at 93°C for 12 hours. Add 8.0gNiCl 2 .6H 2 O and 150ml of toluene, refluxed and separated water for 3h, then filtered, and the filtrate was desolvated under reduced pressure to obtain the catalyst. Industrial production can be scaled up with industrial-grade raw materials.

[0014] Apply this product to Leng 42-Ping 2 heavy oil in Liaohe Oilfield, take an appropriate amount of catalyst, heavy oil and water and put it in a high-pressure reactor. The hydrothermal catalytic cracking reaction will occur at 170℃~200℃, and the quality of the whole system is the benchmark , The amount of catalyst is 0.03~0.1w%, and the amount of water added is more than 25%. After the reac...

Embodiment 2

[0016] 3gC 12 The carboxylic acid was mixed with 1.8g ethylenediamine and the oil bath was heated to 160°C for 3h. The temperature was lowered to 95°C, and an aqueous solution containing 7.5 g of sodium chloroacetate was added. After stirring for 45 minutes, 2.0 g of NaOH was added, and the reaction was continued at 95°C for 11 hours. Add 6.1gNiCl 2 .6H 2 O and 150ml of toluene, refluxed and separated water for 3h, then filtered, and the filtrate was desolvated under reduced pressure to obtain the catalyst. Industrial production can be scaled up with industrial-grade raw materials.

[0017] Apply this product to the heavy oil of Du 813-39-36 in the Liaohe Oilfield, take an appropriate amount of catalyst, heavy oil and water and put it in a high-pressure reactor. The hydrothermal catalytic cracking reaction will occur at 170 ℃ ~ 200 ℃, where the quality of the whole system is As a benchmark, the amount of catalyst is 0.03-0.1w%, and the amount of water added is more than 25%. Af...

Embodiment 3

[0019] 4gC 16 The carboxylic acid was mixed with 1.7g of ethylenediamine and the oil bath was heated to 180°C for 2.5h. The temperature was lowered to 90°C, and an aqueous solution containing 6.5 g of sodium chloroacetate was added. After stirring for 46 minutes, 3.2g of NaOH was added, and the reaction was continued at 90°C for 12 hours. Add 5.5.0g NiCl 2 .6H 2 O and 170ml of toluene, refluxed and separated water for 4h, filtered, and the filtrate was desolvated under reduced pressure to obtain the catalyst. Industrial production can be scaled up with industrial-grade raw materials.

[0020] Apply this product to G540 heavy oil in Henan Oilfield, take an appropriate amount of catalyst, heavy oil and water and put it in a high-pressure reactor. Hydrothermal catalytic cracking reaction will occur at 150℃~200℃. The quality of the entire system is used as the benchmark, and the amount of catalyst is 0.03 ~0.1w%, the amount of water added is more than 25%, the viscosity reduction r...

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PUM

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Abstract

The invention relates to a complex catalyst for viscosity reduction of thick oil by hydrothermal catalytic cracking and application thereof. The complex catalyst is prepared by the following steps of: 1) selecting raw materials: selecting 2 to 3 mass parts of C12-C18 aliphatic carboxylic acid, 1 to 2 mass parts of ethylene dimine, 3 to 5 mass parts of sodium fluoroacetate, 1 to 2 mass parts of sodium hydroxide, 3 to 5 mass parts of nickel chloride hydrate and 140 to 180 mass parts of toluene; and 2) mixing the C12-C18 carboxylic acid and ethylene dimine, then heating to 160 to 180 DEG C in anoil bath and reacting for 2 to 3 hours, cooling to 90 to 95 DEG C, adding sodium chloroacetate-containing aqueous solution, stirring, reacting for 40 to 50 minutes and then adding NaOH, continuously reacting for 10 to 13 hours at the temperature of between 90 and 100 DEG C, finally adding the NiCl2.6H2O and the toluene, refluxing and splitting water for 3 to 5 hours and filtering, and performing reduced pressure desolvation on the filtrate to obtain the catalyst, wherein after the reaction is finished, the viscosity reduction rate of the thick oil reaches over 90 percent, and 9 to 15 percent of heavy component is cracked into a light component.

Description

Technical field: [0001] The invention relates to a complex catalyst for reducing viscosity by hydrothermal catalytic cracking of heavy oil, and its preparation and application. Background technique: [0002] Hydrothermal catalytic cracking is a more effective method for heavy oil exploitation. The technique of hydrothermal catalytic cracking to reduce viscosity for heavy oil exploitation is to inject high-temperature and high-pressure steam into the oil layer while adding appropriate catalysts and other additives to use the formation itself as An inexpensive and available hydrothermal cracking catalytic reactor enables the catalytic cracking of heavy oil under hydrothermal conditions, irreversibly reducing the content of heavy components or changing its molecular structure, and to a certain extent, lighten the heavy oil and reduce The viscosity of heavy oil makes it easy to exploit, gather and process. This is a new idea for heavy oil exploitation. Hydrothermal catalytic cracki...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J31/22C09K8/592C10G11/02
Inventor 陈艳玲逯江毅王元庆杨超
Owner PETROCHINA CO LTD
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