The detection of crane braking descent distance faces numerous challenges in practical engineering applications, primarily due to limitations in the measurement accuracy of existing detection equipment, the complexity of on?site operations, and high equipment costs. A method is proposed to obtain the braking descent distance by using inertial sensors to collect acceleration and angular velocity data during the crane braking process, performing attitude calculation, and combining it with a double integration algorithm. First, a Lagrangian dynamic model of the crane is established to analyze the coupling relationship between the braking descent distance and the equipment environment. Second, a data acquisition device is designed, the detection steps are described, and data synchronous transmission is employed to enhance signal reliability. Finally, the data processing method is investigated, a complete data processing workflow is designed, complex integration algorithms are compared and analyzed, and practical feasibility is verified. The results indicate that this detection method can prevent serious accidents such as load dropping caused by insufficient braking performance, offering superior comprehensive performance, strong feasibility, and promising market prospects.
The spinel?phase Zn2Ga2.98-x Ge0.75O8:Cr0.02, La x (x=0.005,0.010,0.015,0.020,0.025) nanoparticles were synthesized by a hydrothermal method in combination with a subsequent heat treatment. With the La3+ doping concentration increasing from 0 to 0.025, the average particle size of these nanoparticls increased from 64 nm to 78 nm. Under 590 nm excitation, La3+?doped ZGGO nanoparticles exhibited stronger narrow?band NIR emission peaked at 697 nm, originating from the 2E(2G)→4A2(4F) transition of Cr3+. From the TEM and emission spectral analyses, it can be found that the increased NIR persistent luminescence is attributed to the increased particle size and the increased number of luminescent centers in a relatively strong crystal field environment. On the basis of thermoluminescence spectra and the afterglow decay curves, it can be found that La3+ doping leads to the formation of more traps related to the thermal activation process and the afterglow time exceeding 15 h.
In this study, the optical properties of 3D carbon ball were theoretically investigated by using Density?Functional Theory (DFT) and wave function analysis. The electron?leaping mechanism in the Ultraviolet?visible (UV?vis) absorption spectrum was investigated. The electronic excitation properties of 3D carbon ball were investigated by Transition Density Matrix (TDM) and Charge Density Difference (CDD). Raman spectra were calculated and the vibrational modes of the 3D carbon ball were further explained. Meanwhile, the interaction between 3D carbon ball and the external environment was investigated using Electrostatic Potential (ESP), and the degree of electron delocalization of 3D carbon ball was investigated based on the magnetic induction current under the applied magnetic field.It is shown that the absorption spectra of three?dimensional carbon spheres are mainly in the ultraviolet region and that they have a strong electron delocalization capability. This study can provide a theoretical basis for the application of other 3D π?conjugated molecular structures in linear and nonlinear optics.
This paper uses Aspen Plus software to carry out steady?state simulations of a new process for the reactive distillation of hydrogen peroxide isopropylbenzene (CHP) and subsequent refining processes for phenol and acetone. The operating pressure, feed position and number of plates of the reactive distillation column and the refining process were economically optimised with the objective of minimising the total annual cost (CTAC). The results show that the optimal operating parameters of the process are as follows : the total number of trays of RD was 34, the number of trays in the distillation section was 27, the number of trays in the reaction section was 6, the feed position was 28, and the operating pressure was 3.0×104 Pa. The total plate numbers of acetone refining tower (T101), cumene top tower (T102), tar tower (T103) and phenol refining tower (T104) were 25, 61, 23 and 22, respectively. The feed positions are 16, 45, 9 and 9, respectively. The operating pressures were 5.2×104, 5.0×103, 5.5×104, 6.0×103 Pa. The minimum CTAC of the new process was 2 239.03×104 yuan/year. At the same time, the steady?state simulation and economic optimization of the traditional CHP decomposition and subsequent phenol and acetone refining process were also carried out, and the minimum CTAC value was 2 608.13×104 yuan/year. By comparing the reactive distillation process with the traditional process, it can be seen that CTAC can save 14.15% and energy consumption can save 9.01%.