Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method for preparing narrow fraction nontoxic high-purity isohexane

A technology of isohexane and narrow fraction, which is applied in the field of preparation of nontoxic and high-purity isohexane with narrow fraction, can solve the problems of not being able to meet the environmental protection requirements of safe production of nontoxic narrow fraction solvent oil from plant extract oil, and achieve remarkable desulfurization effect, Simple production process and high economic efficiency

Inactive Publication Date: 2010-11-03
CHINA NAT OFFSHORE OIL CORP +1
View PDF1 Cites 12 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Chinese patent 200410027004.5 - the manufacture method of isohexane solvent, has introduced the method that is 60~90 ℃ of solvent oil distillation preparations isohexane by distillation, but its product isohexane content≤95%, and distillation range is relatively wide ( 58~63℃); there is still a gap with the performance requirements of high-purity narrow-fraction isohexane (isohexane content > 95%, distillation range 60-64℃), and it still cannot meet the safety production of plant extract oil and the non-toxic narrow-fraction solvent Environmental requirements for oil

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Method for preparing narrow fraction nontoxic high-purity isohexane
  • Method for preparing narrow fraction nontoxic high-purity isohexane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment Construction

[0015] (1), choose active metal nickel as benzene series catalytic hydrogenation catalyst:

[0016] The active center of the selected catalyst is metal nickel, the shape is cylindrical (Φ5mm×5mm), the bulk density is 1-1.4 liters / kg, and the specific surface area is 95-180cm 2 / kg, strength ≥ 140N / cm, put it in a hydrogenation reactor, when the catalytic reforming raffinate enters the hydrogenation reactor together with industrial hydrogen, it will contact with the catalyst for heterogeneous reaction, and carry out hydrogenation to remove Benzene series.

[0017] (2), catalytic hydrodearomatization and sulfur:

[0018] The raw material catalytic reforming raffinate and industrial hydrogen are preheated to 160°C and simultaneously pumped into the hydrogenation reactor. , Liquid benzene space velocity 0.02 / h, reactor temperature 171°C, inlet hydrogen pressure 1.0Mpa, hydrogenation pressure 1.37Mpa under the conditions of catalytic hydrogenation reaction, dearomatization and de...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to a method for preparing narrow fraction nontoxic high-purity isohexane, which is characterized in that: active metal nickel is used as a benzene catalytic hydrogenation catalyst; catalytic reforming raffinate oil, which has a distilling range of less than or equal to 140 DEG C, aromatic hydrocarbon content of less than or equal to 1.3 percent and sulfur content of less than or equal to 1ppm, and industrial hydrogen are pumped into a hydrogenation reactor to undergo all-component catalytic hydrogenation under conditions of a hydrogen to oil ratio of 5.5-7.5:100, a liquid benzene space velocity of 0.01 to 1 hour, a temperature of 160 to 175 DEG C, a pressure of 0.3 to 1.5MPa and in the presence of the catalyst for dearomatization and desulfuration; the product of the dearomatization and desulfuration is introduced to a dehydrogenation tower, the temperature of the tower is controlled to be 63 to 102 DEG C and light components with a distilling range less than or equal to 60 DEG C are removed; the residual fraction obtained after dehydrogenation is introduced into a heavy component removing tower, and the heavy components of which the distilling range is more than or equal to 75 DEG C are removed; and the fraction (of which the distilling range is 60 to 75 DEG C) left after the removal of the heavy components is introduced into an isohexane tower for fine fractionation, and a fraction obtained at 60 to 64.5 DEG C is the required product. The preparation method has the advantages of relatively mild catalyst operation conditions, obvious dearomatization and desulfuration effects, simple and practical process, stable and reliable product quality and high economic efficiency.

Description

Technical field: [0001] The invention relates to a preparation method of narrow-fraction non-toxic high-purity isohexane, which belongs to the technical field of petrochemical design. Background technique: [0002] Whether it is refined No. 6 solvent oil or high-purity hexane oil, its main component contains hexane. However, as early as 1990, the United States Clean Air Act officially listed n-hexane as one of the 189 air pollutants, affirming that human exposure to n-hexane vapor would damage the central nervous system and motor nerve cells. In 2001, the U.S. Environmental Protection Agency officially announced the standards for the emission of hexane into the atmosphere by oil refineries. Since then, people have paid more attention to the research and development of the oil leaching solvent hexane replacement technology. The oil industry has discussed more than 60 organic solvents, and found that isohexane, isopropanol, ethanol, ethyl acetate and their azeotropic solvents...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
IPC IPC(8): C07C9/16C07C5/13C07C5/10C07C7/04B01J23/755
Inventor 马斐唐善法李国麟夏峥嵘伍锐东刘文正刘忠运岳泉
Owner CHINA NAT OFFSHORE OIL CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products