Comprehensive treatment method and comprehensive treatment apparatus for high-concentration chlorine-containing organic waste gas
A technology for comprehensive treatment of organic waste gas, applied in the direction of gas treatment, separation methods, chemical instruments and methods, etc., can solve the problems of cooling water consumption, reduce operating costs, reduce consumption, and improve economic efficiency
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0029] A chlorobenzene vacuum pump in a chemical plant discharges tail gas with a gas volume of 7865Nm 3 / h, the temperature is normal temperature, the pressure is normal pressure, and the exhaust gas composition is as follows:
[0030]
[0031] Using the method and device of the present invention for treatment, first the waste gas enters the thermal storage oxidation reactor, the oxidation temperature is 600°C, and the flue gas outlet temperature of the oxidation bed is 50°C. Part of the high-temperature flue gas obtained after oxidation is used for the energy self-balancing of the thermal storage reaction. , a part of the high-temperature gas is discharged into the Stirling generator for power generation. After the power generation, the outlet temperature of the flue gas is controlled at 50°C, and the power generation is 35kwh. After this power is passed into the membrane electrolysis reactor, 10kg / h of NaOH lye can be regenerated. The oxidized flue gas is mixed with the ...
Embodiment 2
[0033] Exhaust gas from a chlor-alkali plant in a chemical plant with a gas volume of 12000Nm 3 / h, the temperature is normal temperature, the pressure is normal pressure, and the exhaust gas composition is as follows:
[0034]
[0035] Using the method and device of the present invention for treatment, first the waste gas enters the thermal storage oxidation reactor, the oxidation temperature is 700°C, and the flue gas outlet temperature of the oxidation bed is 60°C. Part of the high-temperature flue gas obtained after oxidation is used for energy self-balancing of the thermal storage reaction , a part of the high-temperature gas is discharged into the Stirling generator for power generation. After the power generation is controlled, the outlet temperature of the flue gas is 90°C, and the power generation is 93kwh. After this power is passed into the membrane electrolysis reactor, 27kg / h of NaOH lye can be regenerated. After the oxidized flue gas is mixed with the flue gas...
Embodiment 3
[0037] Exhaust gas from a chlor-alkali plant in a chemical plant with a gas volume of 10,000Nm 3 / h, the temperature is normal temperature, the pressure is normal pressure, and the exhaust gas composition is as follows:
[0038]
[0039] Using the method and device of the present invention for treatment, first the exhaust gas enters the thermal storage oxidation reactor, the oxidation temperature is 1000°C, the outlet temperature of the oxidation bed flue gas is 80°C, and a part of the high temperature flue gas obtained after oxidation is used for the thermal storage reaction energy self- Balance, part of the high-temperature gas is discharged into the Stirling generator for power generation. After the power generation, the outlet temperature of the flue gas is controlled to 80°C, and the power generation is 114kwh. After this power is passed into the membrane electrolysis reactor, 32kg / h of NaOH lye can be regenerated. The oxidized flue gas and the flue gas after Stirling ...
PUM
Property | Measurement | Unit |
---|---|---|
current density | aaaaa | aaaaa |
current density | aaaaa | aaaaa |
current density | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com