Self-evaporator liquid level measuring device based on dual-pipe air blowing method
A liquid level measurement device and self-evaporator technology, which is applied in the direction of displaying liquid level indicators through pressure measurement, etc., can solve the problems of complicated management procedures, hazards, and high comprehensive cost of use
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2012-07-04
- Estimated Expiration
- Not applicable · inactive patent
Smart Images
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Abstract
Description
technical field
[0001] The invention relates to a self-evaporator liquid level measuring device. Background technique
[0002] At present, in the dissolution section of alumina plants at home and abroad, the liquid level measurement of the self-evaporator is almost always measured by a ray-type liquid level gauge (see attached figure 1 shown). The measurement system usually consists of the following parts:
[0003] a. Radiation source (usually Cs 137 )
[0004] b. Detectors (usually ionization chamber detectors or scintillation detectors)
[0005] c. Transmitter
[0006] The working principle of the measurement system is: use the radiation source to emit a fan-shaped nuclear ray to penetrate the measured medium. Under the condition of a certain density of the measured medium, the higher the liquid level is, the more the nuclear ray is absorbed. The less the amount of radiation, the height of the liquid level is calculated by the transmitter.
[0007] The advantages an...
Examples
Embodiment Construction
[0053] Embodiments of the present invention: it comprises self-evaporator 9, the first blowing pipe 1, the second blowing pipe 2 are connected with self-evaporator 9, two blowing pipes stretch into the bottom of self-evaporator 9, the first blowing pipe 1 and the second blowing pipe The height difference between the bottom ends of the two air blowing pipes 2 is h2; the pipeline connected with the first air blowing pipe 1 is provided with a first air blower 3, a first isolation tank 7, a first differential pressure transmitter 5, and the first air blower 3. The pipeline connected by the two air blowing pipes 2 is provided with a second air blower 4, a second isolation tank 8, and a second differential pressure transmitter 6; the second air blower 3 and the second air blower 4 are connected to the air source .
[0054] The height h2 between the bottom ends of the first blowing pipe 1 and the second blowing pipe 2 is 200-500 mm. Generally take 300mm.
[0055] The first air blow...