Device and method for removing siloxane in dilute sulfuric acid
A technology of dilute sulfuric acid and siloxane, which is applied in the direction of sulfur trioxide/sulfuric acid, etc., can solve the problems of shortening the operation period of the device, difficult cleaning of pipelines and equipment, blockage of pipelines and equipment, etc., and achieves less daily maintenance workload and equipment Easy installation and maintenance, to achieve the effect of filtering function
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0015] A device for removing siloxane in dilute sulfuric acid, which includes a first purifier 7a, a second purifier 7b, a waste liquid collection tank 9, a dilute sulfuric acid storage tank 8, a first purifier initial pressure gauge 5a, a second purifier Initial pressure gauge 5b, end pressure gauge 6a of the first purifier, end pressure gauge 6b of the second purifier, material inlet valve 1a of the first purifier, material inlet valve 1b of the second purifier, backwash valve 4a of the first purifier , the second purifier backwash valve 4b, the first purifier filtrate outlet valve 3a, the second purifier filtrate outlet valve 3b, the first purifier dirt outlet valve 2a, the second purifier dirt outlet valve 2b; One end of the purifier 7a and the second purifier 7b are respectively connected to the first purifier material inlet valve 1a and the second purifier material inlet valve 1b through pipelines, and the tops of the first purifier 7a and the second purifier 7b are respe...
Embodiment 2
[0021] Dilute sulfuric acid enters the first purifier 7a and the second purifier 7b under a pressure of 0.6Mpa;
[0022] Backwashing operation: record the pressure difference between the initial pressure gauge 5a of the first purifier and the final pressure gauge 6a of the first purifier during operation. When the pressure difference reaches 0.4Mpa, start the backwashing system, and use water with a pressure of 0.3Mpa to the first purifier. One purifier 7a is backwashed for 5 seconds; in the same way, record the pressure difference between the second purifier initial pressure gauge 5b and the second purifier end pressure gauge 6b, when the pressure difference reaches 0.4Mpa, start the backwash system, for the second Purifier 7b carries out backwashing operation;
[0023] All the other are with embodiment 1.
Embodiment 3
[0025] Dilute sulfuric acid enters the first purifier 7a and the second purifier 7b under a pressure of 0.7Mpa;
[0026] Backwashing operation: record the pressure difference between the initial pressure gauge 5a of the first purifier and the final pressure gauge 6a of the first purifier during operation. When the pressure difference reaches 0.6Mpa, start the backwashing system, and use water with a pressure of 0.4Mpa to the first purifier. One purifier 7a backwashes for 15 seconds; Similarly, record the pressure difference between the second purifier initial pressure gauge 5b and the second purifier end pressure gauge 6b, when the pressure difference reaches 0.6Mpa, start the backwash system, and the second Purifier 7b carries out backwashing operation;
[0027] All the other are with embodiment 1.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 