scholarly journals DETERMINATION OF THE COEFFICIENT OF HEAT TRANSFER DURING COOLING OF SILVER THERMO PROBES, TAKING INTO ACCOUNT THE EFFECTS OF TEMPERATURE-TIME DELAY

2017 ◽  
Vol 39 (5) ◽  
pp. 41-47 ◽  
Author(s):  
E. N. Zotov ◽  
A. A. Moskalenko A.A. ◽  
O. V. Rasumtseva ◽  
L. M. Protsenko

Existing methods for determining the characteristics of the nonstationary heat transfer process (temperature field, heat transfer coefficient, heat flux density, surface temperature) are considered and analyzed when cooling silver spherical and cylindrical thermo-probes. New analytical solutions are proposed using a special program IQLab, which increase the accuracy of calculations when testing the cooling capacity of various liquids. The results of the calculations are compared with the experimental data.  

2012 ◽  
Vol 512-515 ◽  
pp. 2171-2174 ◽  
Author(s):  
Quan Ying Yan ◽  
Ran Huo ◽  
Li Li Jin

Physical and numerical models of the radiant ceiling cooling system were built and numerically simulated. The results showed that the lower the temperature of cooling water is, the lower surface temperature the ceiling has, and the bigger the cooling capacity is. The bigger the depth of tubes is, the higher the surface temperature and the smaller the cooling capacity. The differences are not evident. The bigger the distance of tubes is, the bigger the surface temperature is and the smaller the cooling capacity is. The diameter of tubes has a few influences on the surface temperature and the cooling capacity. Results in this paper can provide basis and guide for the design of the project, the selection of parameters and the feasibility of the system.


Author(s):  
Zhaowen Wang ◽  
Peng Deng ◽  
Wei Li ◽  
Ronghua Huang

To solve problems such as thermal overload in the cylinder head of a 6-cylinder heavy-duty diesel engine and the thermal cracks in the valve-bridge of the engine. Structure of the coolant jacket was optimized from monolayer to bi-layer, and structures of upper nozzles were also optimized using the orthogonal experimental design method in this paper. At present, the cooling capacity of the coolant jacket in cylinder head is mainly judged by the coolant velocity. In this paper, the coolant heat transfer coefficient (HTC) was adopted as the criterion to evaluate the heat transfer process in cylinder head. Both of the velocity and HTC were used as the evaluation indexes to obtain the optimum schemes respectively. To determine which evaluation index fits the actual heat transfer process better, and which optimized schemes should be adopted, the temperatures in the bottom of the cylinder head were measured. The experimental results show that it is better to evaluate the cooling capacity of coolant jackets by HTC. HTC reflects the actual heat transfer process much better than velocity.


2021 ◽  
Vol 316 ◽  
pp. 282-287
Author(s):  
Boris Yur'ev ◽  
Vyacheslav Dudko

Lime is the product of calcination. Its formation is always related to removal of carbon dioxide generated in the course of carbonate decomposition. Ferrous metallurgy, construction material, chemical and food industry companies account for about 90 % of lime produced in the country. Ferrous metallurgy is the major consumer of commercial lime using up to 40 % of all produced lime. Currently, despite occurrence of new binding and artificially produced chemical compounds, lime remains the major chemical compound produced by the industry in terms of output. Various units (shaft, rotary tubular kilns and fluidized bed kilns) are used for calcination. Shaft kilns are used the most widely. Considering continuously growing demand for lime, the need occurs for intensification of the burning process and optimization of the shaft kiln operating conditions. This requires knowledge of calcination physicochemical and heat transfer process mechanisms. Thus, the work deals with the issues related to determination of the optimal specific fuel consumption for burning of limestone from a particular deposit. It may be done only basing on thermal calculations for an operating shaft kiln, what, in its turn, causes the need for determination of the whole set of limestone and lime heat transfer properties. The obtained work results may be used to optimize the operating conditions of not only shaft but also rotary kilns intended for limestone heat treatment.


2001 ◽  
Vol 47 (10) ◽  
pp. 1821-1828 ◽  
Author(s):  
Jakub Krijt ◽  
Martina Vacková ◽  
Viktor Kožich

Abstract Background: Aminothiols have been implicated in the pathogenesis of arteriosclerosis, and reliable methods are needed to determine their concentrations in body fluids. We present a comparison of two analytical methods and focus on the reduction of low-molecular weight and protein-mixed disulfides of homocysteine, cysteine, cysteinyl-glycine, and glutathione. Methods: The plasma total aminothiol profile was determined by HPLC with fluorescence detection after derivatization with ammonium 7-fluorobenzo-2-oxa-1,3-diazole-4-sulfonate. Disulfides and protein-bound aminothiols were reduced by either tri-n-butylphosphine (the TBP method) or tris(2-carboxyethyl)phosphine (the TCEP method); the effects of temperature, time of reduction, and concentration of reductants were evaluated. Results: The intraassay imprecision (CV) was <3% for all aminothiols using both methods. The interassay CVs for total cysteine (tCys), total cysteinyl-glycine (tCys-Gly), and total homocysteine (tHcy) were <4% and <8% for the TCEP and TBP methods, respectively, whereas for total glutathione (tGSH) the interassay CV was >12% for both methods. Deming regression and Bland–Altman difference plots showed positive biases for total aminothiol concentrations determined by the TCEP method relative to the TBP method. The mean proportional biases were 65%, 27%, 6%, and 60% for tCys, tCys-Gly, tHcy, and tGSH, respectively. The calculated concentrations of total aminothiols by the TCEP method were less influenced by changes in temperature and concentration of reducing agent or by calibrator matrix. Conclusions: The agreement between the TCEP and TBP methods was considerably lower for the determination of tCys, tCys-Gly, and tGSH than for tHcy. For total-aminothiol determination, the TCEP method yields better reproducibility and is more robust than the TBP method.


2019 ◽  
Vol 23 (Suppl. 4) ◽  
pp. 1163-1174
Author(s):  
Slawomir Gradziel ◽  
Karol Majewski ◽  
Marek Majdak

Development of the heat transfer surfaces on the tube inside makes it very difficult or even impossible to determine the heat transfer coefficient analytically. This paper presents the experimental determination of the coefficient in an internally rifled tube with spiral ribs. The tests are carried out on a laboratory stand constructed at the Institute of Thermal Power Engineering of the Cracow University of Technology. The tube under analysis has found application in a supercritical circulating fluidized bed boiler. The heat transfer coefficient local values are determined for the Reynolds numbers included in the range of ~6000 to ~50000 and for three ranges of the heating elements power. As the medium flows through internally rifled tubes with spiral ribs, the heat transfer process gets intensified compared to similar processes taking place in smooth tubes. Based on the obtained experimental data, a correlation is developed enabling determination of the dimensionless Chilton-Colburn j factor. The equation form is selected so that a comparison with existing results of tests performed on rifled tubes can be made. Comparing the Nusselt number values calculated based on the developed correlation with those obtained using other correlations described in the literature, it can be observed that the criterial number is about twice higher. The research results confirm the thesis that the element internal geometry has a sub-stantial impact on the heat transfer process.


2020 ◽  
Vol 76 (1) ◽  
pp. 64-75
Author(s):  
C. Kahra ◽  
F. Nürnberger ◽  
H. J. Maier ◽  
S. Herbst

Abstract For the determination of heat transfer coefficients in air-water spray cooling, two methods are presented that are capable of characterizing multi-nozzle cooling set-ups. The methods are based on the quenching of thin-walled tubes or massive cylinders on which cooling curves are recorded at given positions with thermocouples. The temperature dependent heat transfer coefficients were calculated by an inverse calculation and the measured temperature-time-curves could be reproduced with these data in numerical cooling simulations. Next, the determined heat transfer coefficients were used for the calculation of an air-water-spray quenching process of a forging part with more challenging geometry. The calculated results were compared with thermocouple measurements. Different calculation variants for the heat transfer on component surfaces not directly exposed to the air-water spray are shown and discussed. ◼


1956 ◽  
Vol 186 (2) ◽  
pp. 199-202 ◽  
Author(s):  
Richard W. Schayer

Suspensions of the cells of rat peritoneal fluid have a marked ability to decarboxylate C14 l-histidine and bind the resulting histamine in stable form. The evidence is strong that this activity is due almost entirely to mast cells; these constitute about 4% of the total number of cells present. The effects of temperature, time, and ph on this process were found to be characteristic of enzymic reactions. Preincubation of cell suspensions with nonisotopic histamine had no effect on the formation and binding of C14 histamine; this is evidence that exogenous histamine cannot enter the bound condition in free mast cells. The effects of histidine analogs on binding is described. Disruption of the mast cells results in a considerable loss in histamine forming activity. However, a fairly stable, soluble histidine decarboxylase can be obtained from the disrupted cells. A new method for determination of histamine as the S35 dibenzenesulfonyl derivative is described.


Author(s):  
Yu. P. Morozov

Based on the solution of the problem of non-stationary heat transfer during fluid motion in underground permeable layers, dependence was obtained to determine the operating time of the geothermal circulation system in the regime of constant and falling temperatures. It has been established that for a thickness of the layer H <4 m, the influence of heat influxes at = 0.99 and = 0.5 is practically the same, but for a thickness of the layer H> 5 m, the influence of heat inflows depends significantly on temperature. At a thickness of the permeable formation H> 20 m, the heat transfer at = 0.99 has virtually no effect on the thermal processes in the permeable formation, but at = 0.5 the heat influx, depending on the speed of movement, can be from 50 to 90%. Only at H> 50 m, the effect of heat influx significantly decreases and amounts, depending on the filtration rate, from 50 to 10%. The thermal effect of the rock mass with its thickness of more than 10 m, the distance between the discharge circuit and operation, as well as the speed of the coolant have almost no effect on the determination of the operating time of the GCS in constant temperature mode. During operation of the GCS at a dimensionless coolant temperature = 0.5, the velocity of the coolant is significant. With an increase in the speed of the coolant in two times, the error changes by 1.5 times.


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