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Marine exhaust gas desulfurization purification scrubber

An exhaust gas desulfurization and scrubber technology, applied in the field of scrubbers, can solve problems such as poor desulfurization effect, achieve good catalytic effect, increase catalytic time, and prolong service life.

Pending Publication Date: 2019-02-22
JIANGSU RUIHUA CHEM EQUIP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to overcome the deficiencies of the prior art, provide a scrubber for marine exhaust gas desulfurization and purification, solve the problem of poor desulfurization effect of the marine exhaust gas scrubber in the prior art, and provide a liquid scrubber with good desulfurization effect Scrubber with good gas separation and low liquid discharge pollution

Method used

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  • Marine exhaust gas desulfurization purification scrubber
  • Marine exhaust gas desulfurization purification scrubber
  • Marine exhaust gas desulfurization purification scrubber

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0054] In the above-mentioned scrubber for desulfurization and purification of marine exhaust gas, the width of the V-shaped separation channel 10 is 23mm; the height of the droplet separator is 190mm, the length is 630mm, and the width is 400mm; the height of the desulfurization catalyst plate 7 is 190mm, and the The length of the desulfurization catalyst plate 7 is 630 mm;

[0055] The desulfurization catalyst layer is composed of the following components by weight: 10 parts of aluminum oxide, 5 parts of titanium dioxide, 6 parts of zinc oxide, 3 parts of nickel oxide, 2 parts of zirconium oxide and 3 parts of molybdenum dioxide.

[0056] The preparation method of the desulfurization catalyst layer is: mix aluminum oxide, titanium dioxide, zinc oxide, nickel oxide, zirconium oxide and molybdenum dioxide uniformly according to the proportion of parts by weight, put them into a high-temperature calciner and calcinate at 1000°C for at least 2 hours Finally, the powder particle ...

Embodiment 2

[0059] In the above-mentioned scrubber for desulfurization and purification of marine exhaust gas, the width of the V-shaped separation channel 10 is 25mm; the height of the droplet separator is 200mm, the length is 650mm, and the width is 410mm; the height of the desulfurization catalyst plate 7 is 200mm, and the The length of the desulfurization catalyst plate 7 is 650 mm;

[0060] The desulfurization catalyst layer is composed of the following components by weight: 12 parts of aluminum oxide, 8 parts of titanium dioxide, 8 parts of zinc oxide, 5 parts of nickel oxide, 3 parts of zirconium oxide and 5 parts of molybdenum dioxide.

[0061] The preparation method of the desulfurization catalyst layer is: mix aluminum oxide, titanium dioxide, zinc oxide, nickel oxide, zirconium oxide and molybdenum dioxide uniformly according to the proportion of parts by weight, put them into a high-temperature calciner and calcinate at 1200°C for at least 2 hours Finally, the powder particle ...

Embodiment 3

[0064] In the above-mentioned scrubber for marine exhaust gas desulfurization and purification, the width of the V-shaped separation channel 10 is 23mm; the height of the droplet separator is 200mm, the length is 640mm, and the width is 410mm; the height of the desulfurization catalyst plate 7 is 200mm, and the The length of the desulfurization catalyst plate 7 is 640mm;

[0065] The desulfurization catalyst layer is composed of the following components by weight: 11 parts of aluminum oxide, 7 parts of titanium dioxide, 7 parts of zinc oxide, 4 parts of nickel oxide, 3 parts of zirconium oxide and 5 parts of molybdenum dioxide.

[0066] The preparation method of the desulfurization catalyst layer is as follows: mix aluminum oxide, titanium dioxide, zinc oxide, nickel oxide, zirconium oxide and molybdenum dioxide according to the proportion of parts by weight, put them into a high-temperature calciner and calcinate at 1100°C for at least 2 hours Finally, the powder particle siz...

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Abstract

The invention relates to the technical field of scrubbers and in particular relates to a marine exhaust gas desulfurization purification scrubber. The scrubber comprises a tank body, a scrubbing device and a liquid storage tank, wherein the scrubbing device and the liquid storage tank are arranged inside the tank body; the liquid storage tank is arranged at the lower part of the scrubbing device;the tank body comprises an inlet, an exhaust pipe, a drainage pipe and an outlet; the scrubbing device refers to at least two groups of baffle plates fixed into a whole by virtue of wide positioning blocks; a desulfurization catalyst plate is a desulfurization catalyst layer formed by uniformly spraying a desulfurization catalyst on the surface of a metal plate; the baffle plates are at least twogroups of liquid drop separators which are detachably connected into a whole by virtue of first positioning blocks; and the liquid drop separators are composed of at least two separation channels in fixed connection by virtue of second positioning blocks. The invention solves the problem in the prior art that a marine exhaust gas scrubber is poor in desulfurization effect, and provides the scrubber with advantages of being excellent in desulfurization effect, excellent in liquid-gas separation effect and small in pollution of discharged liquids.

Description

technical field [0001] The invention relates to the technical field of scrubbers, in particular to a scrubber for marine exhaust gas desulfurization and purification. Background technique [0002] Desulfurization has always been a difficult problem in the control of ship exhaust gas pollution. Annex VI of MARPOL 73 / 78, one of the international maritime environmental conventions, and the Implementation Plan for Ship Emission Control Areas in the Pearl River Delta, Yangtze River Delta, and Bohai Rim (Beijing-Tianjin-Hebei) Waters issued by the Ministry of Transport of China in 2015, all have regulations on ship exhaust. The upper limit of the sulfur limit must meet the strict requirements of different standards of 0.1% and 0.5%. [0003] At present, ship exhaust gas scrubbing and desulfurization systems (EGCS) are mainly divided into two categories: dry scrubbing and desulfurization systems and wet scrubbing and desulfurization systems. Due to the special requirements of shi...

Claims

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Application Information

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IPC IPC(8): B01D53/86B01D53/50B01D45/04
CPCB01D45/04B01D53/8609B01D2259/4566
Inventor 秦松王平
Owner JIANGSU RUIHUA CHEM EQUIP CO LTD
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