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Isooctane production line

A production line, isooctane technology, applied in the direction of hydrocarbons, chemical instruments and methods, organic chemistry, etc., can solve the problems of poor control of reflux tank drainage, low working efficiency of raw material buffer tank, and reflux tank cooling efficiency No high problems, to achieve the effect of improving cooling effect, improving flash evaporation effect and reasonable structure

Active Publication Date: 2017-06-09
荆门市渝楚化工有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] At present, through refining and a series of reactions, petroleum gas can obtain isooctane, which is the main compound used to blend base gasoline. The combustion and antiknock properties of gasoline with isooctane can be greatly improved. During the reaction in the propane tower, the mixed gas generated by the reaction needs to be cooled into a liquid state through the reflux tank and recycled to the depropanizer for secondary separation. The cooling efficiency of the existing reflux tank is not high, and the discharge of the reflux tank cannot be well controlled. It is easy to discharge the mixed gas in the tank directly to the depropanizer, resulting in energy waste. The existing raw material buffer tank and flash tank have low working efficiency, which makes the working efficiency of each reaction stage of isooctane low.

Method used

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Embodiment Construction

[0013] Such as figure 1 , 2 , 3, 4, and 5, the present invention includes refrigerant pump 10, raw material buffer tank 11, depropanizer 12, reflux tank 13, dehydrator 20, reactor 21, flash tank 22, pickling settling chamber 23, Alkali washing settling chamber 24, de-isobutanizer 25 and de-butanizer 26, raw material buffer tank 11 includes a tank shell 15 and a group of partition plates 16, and the tank shell 15 is respectively provided with an air inlet and a condensing agent inlet and the liquid outlet, a group of partition plates 16 are respectively installed in the tank shell 15, and the tank shell 15 is divided into a plurality of semi-closed cavities, and a guide is provided between the two adjacent partition plates 16. Air plate 18, both sides of air guide plate 18 are welded in the tank shell 15, and the upper and lower ends of the air guide plate 18 are respectively provided with a gap with the inner wall of the tank shell 15, and the tank shell 15 is provided with a...

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PUM

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Abstract

The invention discloses an isooctane production line. The isooctane production line comprises a coolant pump (10), a raw material buffer tank (11), a depropanization tower (12), a return tank (13), a dehydrater (20), a reactor (21), a flash tank (22), a pickling settling chamber (23), an alkali wash settling chamber (24), a deisobutanizer (25) and an n-butane removal tower (26), wherein the raw material buffer tank (11) comprises a tank shell (15) and a group of separators (16). The isooctane production line disclosed by the invention has the advantages that due to the group of separators in the buffer tank, the gas flow time in the buffer tank is increased, and the liquefaction efficiency is improved; the tank body is separated into an upper part and a lower part by a spherical separator, so that the contact area between mixed gases and condensing agents is enlarged by the spherical separator, and the cooling effect is improved; the flash effect is improved by changing the contact area and time between liquid in the flash tank and air; and the whole production line is reasonable in structure and high in efficiency.

Description

technical field [0001] The invention relates to the technical field of petroleum gas deep processing, in particular to an isooctane production line. Background technique [0002] At present, through refining and a series of reactions, petroleum gas can obtain isooctane, which is the main blending substance used to blend base gasoline. The combustion and antiknock properties of gasoline with isooctane can be greatly improved. During the reaction in the propane tower, the mixed gas generated by the reaction needs to be cooled into a liquid state through the reflux tank and recycled to the depropanizer for secondary separation. The cooling efficiency of the existing reflux tank is not high, and the discharge of the reflux tank cannot be well controlled. It is easy to discharge the mixed gas in the tank directly to the depropanizer, resulting in waste of energy. The existing raw material buffer tank and flash tank have low working efficiency, which makes the working efficiency o...

Claims

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Application Information

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IPC IPC(8): C07C7/00C07C7/04C07C9/16
CPCC07C7/005C07C7/04C07C9/16Y02P20/10
Inventor 肖鹏
Owner 荆门市渝楚化工有限公司
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