Emergent shutdown method for hydrogenation device in production of hydrogen peroxide
An emergency shutdown, hydrogen peroxide technology, applied in chemical instruments and methods, peroxide/peroxy hydrate/peroxyacid/superoxide/ozonide, inorganic chemistry, etc., can solve hydrogenation liquid flash explosion, Catalyst agglomeration, danger and other problems to achieve the effect of preventing excessive hydrogenation, protecting the catalyst and preventing accidents
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2016-06-01
Smart Images
Figure 1
Abstract
Description
Technical field
[0001] The invention relates to a method for emergency shutdown of a hydrogenation device in hydrogen peroxide production. Background technique
[0002] Hydrogen peroxide is a colorless and transparent liquid, which can be miscible with water in any ratio. Hydrogen peroxide is a strong oxidant, which is extremely unstable. When it comes in contact with heavy metals and their salts, dust, and alkaline substances, it can be exposed to light or heat. It accelerates decomposition and releases a lot of heat. Contact with hydrogen peroxide on rough surfaces may also accelerate its decomposition. The decomposition reaction is as follows: H 2 O 2 —→H 2 O+1 / 2O 2 +97.8kj / mol. The decomposition reaction speed is closely related to temperature, pH value and impurity content. With the increase of temperature, pH value and its impurity content, the decomposition reaction speed also increases.
[0003] The industrial production method of hydrogen peroxide is mainly the anthraqui...
Examples
Embodiment
[0032] The emergency shutdown system using this hydrogenation system, hydrogen 1 is 105Nm 3 / h, working fluid 4 is 3.12m 3 / h, circulating working fluid 6 is 0.71m 3 / h, the total working fluid 7 is 3.83m 3 / h. When the emergency hydrogenation shutdown system is turned on, first start the emergency shutdown system 14 of the hydrogenation system, and instantly close the hydrogen feed valve K1; open the valve K6 of the working fluid circulation pipeline, and close the valve K7 that discharges the working fluid to the next process. The working fluid is circulated at 100%; when the outlet temperature of the hydrogenation tower drops to 45°C, open the bypass valve K5 of the working fluid, close the valve K4 where the working fluid enters the hydrogenation tower; open the valve K2 of the low-temperature aromatics feed line to the hydrogenation tower Introduce 48℃ low-temperature aromatic hydrocarbons, wash the catalyst bed for 3 minutes, and then introduce 40℃ low-temperature aromatic...