Long chain paraffin hydrogenation heterogeneous condensation freezing point depressing method and catalyst thereof

A technology for hydrogenation of isomerized and long-chain alkanes, applied in the energy field, can solve the problems of limited use, not too obvious effect, low enough freezing point, etc., and achieves reduction of secondary reactions and cracking reactions, small crystal particles, and reduced production. cost effect

Inactive Publication Date: 2013-02-27
DALIAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Generally speaking, the combination of ZSM-48 and other molecular sieves (such as Beta) can obtain better hydroisomerization performance, but the current research is only to apply the molecular sieve catalyst mainly based on ZSM-48 to the production of lubricating oil
Hydrotreated vegetable oil contains a large amount of long-chain alkanes, which can be added to gasoline and diesel oil as a blending component. Since the long-chain alkanes are mainly straight-chain alkanes, the freezing point is not low enough, which greatly limits the use in cold regions. usage of
Chinese patent 201110425819.9 introduces the hydrogenation treatment of vegetable oil. Although the patent also involves the isomerization depressing treatment of gasoline and diesel components after hydrogenation, the effect is not too obvious.
However, the use of ZSM-48 as the main molecular sieve catalyst to carry out isomerization and depreciation of gasoline and diesel components obtained after vegetable oil hydrotreating has not yet been reported.

Method used

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  • Long chain paraffin hydrogenation heterogeneous condensation freezing point depressing method and catalyst thereof
  • Long chain paraffin hydrogenation heterogeneous condensation freezing point depressing method and catalyst thereof
  • Long chain paraffin hydrogenation heterogeneous condensation freezing point depressing method and catalyst thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0014] Preparation of different Pt / ZSM-48 catalysts. Three kinds of ZSM-48 molecular sieves with silicon-aluminum molar ratios of 33, 96, and 165 were ion-exchanged with 1mol / L ammonium nitrate aqueous solution, and repeated three times to keep the volume of ammonium nitrate aqueous solution and the mass ratio of molecular sieves at 20:1. After that, it is baked into a hydrogen ZSM-48 molecular sieve under the air atmosphere condition of 550°C to ensure that the weight content of sodium ions in the molecular sieve is less than 0.5%. The supported Pt catalyst was prepared by the equal volume impregnation method. The metal Pt precursor used was chloroplatinic acid, and the weight of metal Pt accounted for 0.4% of the total weight of the catalyst. After impregnation, three different Pt catalysts were obtained by drying, roasting and reduction. / ZSM-48.

Embodiment 2

[0016] Preparation of Pt / Beta, Pt / ZSM-23, Pt / ZSM-22, Pt / Y catalysts. The silicon-aluminum molar ratios of the selected Beta, ZSM-23, ZSM-22, and Y molecular sieves are 32, 46, 87, and 12, respectively. The supported Pt catalyst was prepared according to the experimental procedure described in Example 1, the metal Pt precursor used was potassium chloroplatinate, and the weight of the metal Pt accounted for 0.4% of the total weight of the catalyst.

Embodiment 3

[0018] Preparation of Pt-Pd / ZSM-48 and Pt-Ru / ZSM-48 bimetallic catalysts. Two ZSM-48 molecular sieves with a silicon-aluminum molar ratio of 120 were ion-exchanged with 1.0mol / L ammonium nitrate aqueous solution, and repeated three times to keep the volume of ammonium nitrate aqueous solution and the mass ratio of molecular sieves at 20:1. Calcined into hydrogen type ZSM-48 molecular sieve under the condition of air atmosphere at 550°C to ensure that the weight content of sodium ions in the molecular sieve is less than 0.5%. Adopt equal volume impregnation method to prepare supported bimetallic catalyst, impregnate metal Pd or Ru earlier, the metal Pd precursor that adopts is palladium nitrate, the metal Ru precursor is ruthenium trichloride, and the weight of metal Pd or Ru accounts for 10% of the total catalyst weight 0.2%, drying and roasting after impregnation, and then impregnating metal Pt, the metal Pt precursor used is chloroplatinic acid, and the weight of metal Pt ac...

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Abstract

The invention relates to a long chain paraffin hydrogenation heterogeneous condensation freezing point depressing method and a catalyst thereof and belongs to the technical field of energy. A single-section or two-section serial connection hydrogenation heterogeneous process is adopted; raw oil and hydrogen pass through a hydrogenation heterogeneous catalyst bed layer, wherein the raw oil comprises vegetable oil, Fischer-Tropsch wax oil or waste lubricating oil which are hydrogenated; and an obtained hydrogenation heterogeneous product has the characteristics of low freezing point, high cetane number and the like. An adopted hydrogenation heterogeneous condensation freezing point depressing catalyst is a molecular sieve catalyst, and comprises a molecular sieve carrier and a metal active component. The total weight of a molecular sieve is 20 weight percent to 90 weight percent of the weight of the molecular sieve carrier, and the weight of the metal active component is 0.05 weight percent to 0.5 weight percent of the total weight of the total catalyst. The process is simple, the operation is stable, the freezing point of the raw oil can be effectively reduced to 10DEG C below zero to 20DEG C below zero by selecting appropriate hydrogenation heterogeneous conditions, so that the fluidity of an oil product at low temperature is ensured, and wide industrial application prospect is realized.

Description

technical field [0001] The invention belongs to the technical field of energy, and relates to a method for decondensation through hydroisomerization of long-chain alkanes. More specifically, molecular sieve catalysts are used to hydroisomerize long-chain alkanes in hydrotreated vegetable oil or coal tar under suitable process conditions to reduce the freezing point of oil products so that they can be processed in low temperature environments. be more widely used. Background technique [0002] Hydroisomerization of alkanes is one of the important reactions in the petroleum refining process, and it is mainly used in the production of high-quality fuel oil and high-grade lubricating oil. Among them, the hydroisomerization of light alkanes can produce high-octane gasoline blending components, while the hydroisomerization of long-chain alkanes is mainly used to improve the quality of middle distillates (jet fuel and diesel) and lubricating oils. low temperature flow properties....

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G45/64B01J29/74B01J29/12
Inventor 梁长海汪镭李闯陈霄张淼
Owner DALIAN UNIV OF TECH
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