Modeling method of energy dissipation regulation model under miha pure pneumatic operating conditions
A technology of purely aerodynamic conditions and operating conditions, applied in chemical machine learning, chemical process analysis/design, chemical data mining, etc., can solve problems such as limited desulfurization rate and difficult sulfur removal
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0080] S100. Analyze the bubble generation process under pure pneumatic conditions, and establish an energy conversion model in the bubble breaker;
[0081] Before gas was introduced, the bubble breaker was filled with static reaction liquid. When the gas starts to be introduced, due to the gas pressure P G and system operating pressure P m There is a pressure difference ΔP between them, the static pressure of the gas will be transferred to the liquid, causing the liquid to turbulent, and the gas itself pressure will quickly reduce to the operating pressure in the MIHA. Due to the gas-liquid two-phase flow, the gas-liquid flows out from the bubble breaker. For pneumatic operating conditions, the liquid flow Q L much smaller than the gas flow Q G , the energy required for the operation of the system is almost entirely provided by the gas pressure energy.
[0082] build as figure 1 The physical model diagram shown is:
[0083] It is assumed that the liquid in the system i...
Embodiment 2
[0146] This embodiment specifically describes the energy dissipation regulation model constructed based on the method of Embodiment 1.
[0147] The energy dissipation regulation model obtained based on the modeling method of Example 1 is as follows:
[0148]
[0149]
[0150]
[0151]
Embodiment 3
[0153] In this example, based on the modeling method of Example 1, the supply pressure difference ΔP and the ventilation rate Q are studied for the specific reactor structure and reaction system. G to the energy dissipation rate ε mix Impact.
[0154] (1) Supply air pressure difference ΔP versus energy dissipation rate ε mix Impact;
[0155] The calculation conditions are as follows:
[0156] Crusher diameter D 1 =0.02m; the ratio of the diameter of the bubble breaker nozzle to the diameter of the breaker K 1 =0.5;
[0157] Residue density ρ L =800Kg / m 3 ;Operating pressure P m =14MPa; supply pressure difference ΔP=1~10MPa; gas temperature T=450℃.
[0158] Supply air pressure difference ΔP versus energy dissipation rate ε mix impact such as figure 2 shown (ventilation volume 80L / h);
[0159] (2) Supply air pressure difference ΔP versus gas holdup φ G Impact;
[0160] The calculation conditions are the same as (1); the results are as follows image 3 shown;
[...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


