scholarly journals MULTI-PURPOSE CHISEL FOR SOIL TREATMENT IN VINEYARDS

Russian vine ◽  
2021 ◽  
Vol 17 ◽  
pp. 31-39
Author(s):  
G.G. Parkhomenko ◽  
◽  
S.I. Kambulov ◽  
◽  
◽  
...  

Used in Russia mechanized technology in the vineyards characterized by an increase in en-ergy costs 2.5–3.4 times compared to foreign countries. Most of the energy costs account for processing vineyard soil. It is necessary to improve the methods of mechanized soil cul-tivation in vineyards in terms of reducing en-ergy consumption while maintaining quality. The aim of the study is to develop mecha-nized universal technical means and working bodies for processing row-spacing of vine-yards with the lowest energy consumption without damaging the root system of the bushes. The designed multioperational chisel is capable of performing tiered tillage in ac-cordance with the architectonics of the root system of the bushes. Loosening depth 9–45 cm. The original design of the working bodies of the chisel with an additional degree of freedom provides a reduction in traction resistance by 12–14% and specific energy consumption by 1.2 and more times. Chisel complies with agrotechnical requirements in terms of fulfilling the quality indicators of the technological process. The number of frac-tions up to 50 mm 57.5–76.5 %, lumps over 100 mm 8–9 %. Universal design multiopera-tional garden and vineyard chisel allow its use in technologies of cultivation not only fruit, but also grain and row crops.

2021 ◽  
Vol 937 (2) ◽  
pp. 022095
Author(s):  
G Parkhomenko ◽  
S Kambulov ◽  
E Zubrilina ◽  
O Babenko ◽  
L Vysochkina

Abstract The mechanized technologies applied in Russia in vineyards are characterized by 2.5-3.4 times higher energy costs comparing to foreign countries. It is necessary to improve the methods of mechanized tillage in vineyards in order to reduce energy costs while maintaining quality. The purpose of the study is to develop mechanized universal technical means and working bodies for processing vineyard rows with the lowest energy consumption without damaging the root system of the bushes. The designed multi-stage chisel is capable of performing multi-tiered tillage in accordance with the architectonics of the root system of the bushes. The depth of loosening is 9-45 cm. The original design of the working bodies of the chisel with the additional degree of freedom provides reduction in traction resistance by 12-14% and specific energy consumption by 1.2 and more times. Chisel complies with agrotechnical requirements for the implementation of quality indicators of the technological process. The number of fractions of up to 50 mm is 57.5-76.5%, lumps of over 100 mm is 8-9%. The versatile design of the multi-operational horticultural and vineyard chisel will allow it to be used in the cultivation technologies of not only fruit and berry, but also grain and row crops.


2020 ◽  
Vol 2 (38) ◽  
pp. 46
Author(s):  
E. Berezhenko

Improving the technological efficiency of the machines for harvesting root crops by reducing the energy costs of the process of harvesting the main array of hills is an urgent task. The solution to this problem is possible through the development of new energy-saving methods of assembly of the main array of hills and improved designs of hock-harvesting modules. The article provides an analysis of the methods of harvesting hogs and working bodies of harvesting modules. On the basis of the analysis, an energy-saving method of assembling the main array of the ridge and a scheme of an improved jerking module are proposed.Key words: rotary cutter, auger, guide channel, dividing disk, laying of a twig, row spacing of root crops.


2021 ◽  
Vol 51 (2) ◽  
pp. 395-401
Author(s):  
Vladimir Kharitonov ◽  
Vladimir Asafov ◽  
Pavel Kuznetsov ◽  
Valentina Gabrielova

Introduction. One of the promising methods in the production of dairy and other food in concentrated, condensed and dry forms is a consistent combination of dehydration methods. The subject of this research relevant now is approaches to the calculation of such processes. The work objective is to analyze the dehydration staging effect on the energy consumption in this process. Study objects and methods. Liquid, concentrated and powdered dairy products: whole and skim milk, milk whey, whole milk substitutes, as well as their dehydration parameters at certain stages. The determination of moisture and solids mass fraction in products was carried out with a standard method. Results and discussion. The feasibility of using a multi-stage dehydration method for the production of various types of powder milk products has been justified. The characteristic boundaries of solids mass fraction at different stages of the process were determined. The material-balance equation made it possible to define the formula for the total specific energy consumption relative to the unit of the final dry product at an arbitrary number of dehydration stages. The paper contains examples of a comparative efficiency assessment of the dehydration process carried out at different stages from the point of view of energy costs of its implementation. Conclusion. The research featured various issues related to the use of dehydration methods in the production of milk powder products. An equation has been drawn up to estimate the specific energy consumption of the multi-stage dehydration process relative to a unit of the final dry product. The use of a multi-stage process allows to effectively reduce the specific energy consumption, as well as to generate new high quality products.


2020 ◽  
Vol 20 (3) ◽  
pp. 302-310
Author(s):  
Yu. M. Lyashenko ◽  
E. A. Revyakina ◽  
A. Yu. Lyashenko

Introduction. The creation of new types of bucket working bodies of excavators through synthesizing technical solutions to improve the transporting functions of the bottom is considered. These solutions are based on reducing the resistance and energy consumption under digging-in and scooping due to the transition from sliding friction to rolling friction during the movement of the rock mass along the bottom of the bucket.Materials and Methods. Analysis of the bulk materials handling processes using existing loading appliances identified design flaws that affect the efficiency of their operation. Advanced design diagrams of loading bodies were searched on the basis of the accumulated experience and the study of the morphological features of the existing equipment. Combinatorial analysis of possible combinations of elements with their various qualitative compositions, mutual arrangement, imposed links, and synthesis of new technical solutions for loading and transportation modules are carried out. Results. The results of the morphological synthesis implementation were the systematization and development of designs of bucket working bodies with a bottom in the form of a roller surface and a closed belt, as well as with a conveyor-type drive mechanism. The application of rollers as a supporting surface of a loaded rock mass causes a decrease in friction forces and in the power capacity of the work process. In addition, rotating rollers provide uniform abrasion of the working surface, which increases significantly the time to the equipment breakdown and increases the process efficiency. Working bodies with a drive mechanism make it possible to activate the interaction of the conveyor bottom in the form of a closed belt with the rock mass and, as a result, to accelerate the process of filling the bucket container.Discussion and Conclusions. The bucket working bodies described in the paper compare favorably with existing analogues in that they provide a reduction in the time to digging-in, scooping and unloading, a decrease in specific energy consumption, an increase in bucket filling, which ultimately contributes to an increase in productivity. A slight increase in the structural complexity and cost of the working body causes additional capital costs, which are paid back within two to four months.


Author(s):  
Д.В. Бастриков ◽  
Ю.Н. Власов ◽  
С.В. Кучер ◽  
Д.Е. Куницкая

В статье приводятся результаты экспериментов по измельчению отходов окорки ели в промышленном измельчителе Erdwich M600/1-400. В опытах использовали три группы влажности отходов: отходы непосредственно после окорки (относительная влажностью 70%), подсушенные на воздухе (относительная влажность 40%) и высушенные в сушильной камере (относительная влажность 10%). Средняя крупность кусков до измельчения составляла 70, 50 и 30 мм. Работу, совершенную во время измельчения материала, рассчитывали по зафиксированным данным о потребляемой силе тока при известном напряжении в сети. Установлена закономерность для оценки затрат энергии, требующейся для измельчения отходов окорки ели в зависимости от их относительной влажности и степени измельчения. Показано, что удельная энергоемкость измельчения отходов окорки ели связана с относительной влажностью отходов окорки и степенью их измельчения нелинейной зависимостью, повторяющей структуру закона измельчения Кирпичева-Кика. Отношение теплоты сгорания сухого вещества, содержащегося в продукте измельчения коры ели («энергетическая стоимость»), и энергии, затраченной на ее измельчение («энергетическая себестоимость»), нелинейно зависит от относительной влажности коры, причем у зависимости есть точка экстремума, а именно - минимума. Оптимальная по этому соотношению влажность отходов окорки ели, подлежащих измельчению, составляет 25%. Удельная энергоемкость измельчения отходов окорки ели при оптимальной влажности пропорциональная натуральному логарифму степени измельчения, формула (8). При оптимальной влажности для измельчения отходов окорки ели в 5-15 раз потребуется затратить энергию, составляющую 5-10% теплоты сгорания. В заключение также приводятся предложения о перспективных направлениях дальнейших исследований дробления древесных материалов. The article presents results of experiments on shredding of debarking waste with an industrial shredder Erdwich M600 / 1-400. The experiments use three groups of waste’s humidity: waste immediately after debarking (relative humidity 70%), dried in air (relative humidity 40%) and dried in the drying camera (relative humidity 10%). The average size of the pieces before shredding was 70, 50 and 30 mm. The results set a pattern for evaluating the energy costs required for shredding of debarking waste depending on the relative humidity and the shredding ratio. The results prove that the energy consumption of debarking waste shredding associates with relative humidity of the waste and shredding ratio with a nonlinear dependence, which repeats structure of the Kirpichev-Kik dependence. The paper proves that the caloric value of dry matter contained in the shredding product, and the energy expended in its shredding, link each other as a nonlinear function of the bark humidity with optimal humidity of 25%. The specific energy consumption of the debarking waste shredding at the optimal humidity is proportional to the natural logarithm of the shredding ratio. At the optimal humidity of debarking waste shredding with ratio 5-15 requires expending energy around 5-10% of the waste caloric value. The paper also contains suggestions about further prospective research in the field of wooden materials shredding.


Author(s):  
M. A. Promtov ◽  
S. E. Kutukov ◽  
A. N. Koliukh ◽  
F. S. Zverev

The regularities of changes in energy consumption to reduce the viscosity of highly paraffinic oil during processing in an installation based on a rotary impulse apparatus (RIA) are experimentally investigated. The decrease in oil viscosity during processing in RIA exceeds 40%. An increase in the amount of oil supply to the RIA makes it possible to reduce the specific energy consumption for its processing at the same relative value of the decrease in viscosity. Specific energy consumption decreases with an increase in oil consumption through the RIA according to the dependence close to the logarithmetic one.


Foods ◽  
2019 ◽  
Vol 8 (6) ◽  
pp. 198 ◽  
Author(s):  
Julien Chamberland ◽  
Dany Mercier-Bouchard ◽  
Iris Dussault-Chouinard ◽  
Scott Benoit ◽  
Alain Doyen ◽  
...  

Ultrafiltration (UF) and microfiltration (MF) are widely-used technologies to standardize the protein content of cheesemilk. Our previous work demonstrated that protein retention of a 0.1-µm MF spiral-wound membrane (SWM) was lower, but close to that of a 10 kDa UF one. Considering that the permeability of MF membranes is expected to be higher than that of UF ones, it was hypothesized that the former could improve the efficiency of the cheesemaking process. Consequently, the objectives of this work were to compare 0.1-µm MF and 10 kDa UF spiral-wound membranes in terms of (1) hydraulic and separation performance, (2) energy consumption and fouling behavior, (3) cheesemaking efficiency of retentates enriched with cream, and (4) economic performance in virtual cheesemaking plants. This study confirmed the benefits of using MF spiral-wound membranes to reduce the specific energy consumption of the filtration process (lower hydraulic resistance and higher membrane permeability) and to enhance the technological performance of the cheesemaking process (higher vat yield, and protein and fat recoveries). However, considering the higher serum protein retention of the UF membrane and the low price of electricity in Canada, the UF scenario remained more profitable. It only becomes more efficient to substitute the 10 kDa UF SWM by the 0.1-μm MF when energy costs are substantially higher.


2019 ◽  
Vol 124 ◽  
pp. 05054 ◽  
Author(s):  
A.K. Apazhev ◽  
A.G. Fiapshev ◽  
Iu.A. Shekikhachev ◽  
L.M. Khazhmetov ◽  
A.L. Khazhmetova ◽  
...  

To ensure the food security of the Russian Federation, one of the priority areas of the state’s economic and food policy is a step-by-step reduction of the dependence of the domestic agroindustry complex on the import of technologies, machines, and equipment. Currently, machines and aggregates that perform one specific operation are often used in preparing the soil for sowing crops; their multiple passes along the surface of the field being treated increase energy costs, lead to soil compaction, emergence and development of erosion processes. Considering this, further improvement of cultivation technologies, machines and units for soil preparation and sowing crops is required. To solve this problem, we propose an improved technology and an optimized complex of machines that can perform plowing, crushing soil blocks, mulching the topsoil, and sowing. The use of the proposed technology and an optimized machinery complex for the cultivation of winter wheat in the Central part of the North Caucasus resulted in a decrease in: direct energy costs by 33.5%; living labor costs by 31.7%; specific energy consumption of MTA by 41.7%; materialized energy costs by 50%; energy consumption for sowing by 7.7%. As a result, total energy costs decreased by 34%.


The article presents the results of driving and static tests of pile models with different longitudinal shapes, carried out in laboratory conditions. It was revealed that the specific energy consumption of driving a pyramidal-prismatic pile can either exceed or be less than the specific energy consumption of driving a prismatic pile. Unlike pyramidal piles, pyramidal-prismatic piles have less specific energy consumption for driving. Energy costs for driving pyramidal-prismatic piles, as well as their resistance to pressing vertical loads depend on the length of the pyramidal section and rise with its increase. It has been established that, with the same depth of driving and with the same piles, the specific bearing capacity of the pyramidal-prismatic piles is higher than the prismatic piles and less than the pyramidal pile. The revealed features of the behavior of the pyramidalprismatic piles are due to the influence of the longitudinal shape and the length of the pyramidal part of their shaft on the driving process and behavior under the loads.


2019 ◽  
pp. 162-167
Author(s):  
Aleksandr Vasylyk ◽  
Anatoly Yalanetskiy

Приведены основные схемы получения молодых коньячных дистиллятов на аппаратах периодического действия двойной сгонки (шарантского типа), традиционно применяемые в отечественном коньячном производстве и у классических французских производителей. При помощи математического моделирования проведен анализ и определен выход коньячного дистиллята с заданными кондициями и удельные энергетические затраты при одинаковых начальных условиях, но при различных вариантах перегонки. Произведен расчет кондиций основных получаемых продуктов и промежуточных фракций за один цикл дистилляции, а также за длительную последовательность циклов для учета влияния возвращаемых головных и хвостовых фракций, на процесс последующих перегонок. Установлено, что схемы получения коньячных дистиллятов, традиционно используемые в странах СНГ, и метод дистилляции MARTELL, являются менее эффективными с точки зрения выхода коньячного дистиллята и удельных энергозатрат, чем метод дистилляции коньячных домов REMY MARTIN и HENNESSY. Установлено, что регулирование объемной доли этилового спирта в спирте-сырце коньячном за счет отбора хвостовой фракции при первой перегонке является эффективным способом управления процессом дистилляции, который оказывает влияние на общий выход кондиционного коньячного дистиллята и удельные энергетические затраты. Максимальный выход коньячного дистиллята и минимальные удельные энергозатраты при перегонке виноматериала с объемной долей этилового спирта 10,5 % и получением коньячного дистиллята с объемной долей этилового спирта 70% достигаются в случае начала отбора хвостовой фракции при объемной доле этилового спирта в парах (спиртовом фонаре) в диапазоне 14-16%. Показано, что применяемые различными производителями схемы получения коньячных спиртов имеют потенциал для оптимизации, позволяющий увеличить выход коньячного спирта до 2,4 % и снизить удельные энергозатраты до 5 %. Оптимизация схемы получения коньячных дистиллятов не требует дополнительных капиталовложений и может служить дополнительным источником прибыли без какой-либо модернизации оборудования.The paper describes basic schemes for producing young brandy distillates on double distillation batch machines (charente type) traditionally used in domestic brandy production and by traditional French producers. Mathematical modelling was used to analyze and determine the output of brandy distillate with predetermined parameters and specific energy costs under the same initial conditions, but with different distillation options. We calculated quality parameters of the main resultant products and intermediate fractions during one distillation cycle, as well as during the long cycle sequence to estimate the effect of returned fraction heads and tails on the subsequent distillation process. The analysis established that brandy distillate production schemes traditionally used in the CIS countries and the MARTELL distillation method are less effective in terms of brandy distillate output and specific energy consumption as compared to the REMY MARTIN and HENNESSY cognac distillation method. It was established that control of the volume fraction of ethyl alcohol in the raw brandy alcohol by tail fraction takeoff during the first distillation is an effective way to control the distillation process, which affects the overall output of conditioned brandy distillate and specific energy costs. The maximum brandy distillate output and the minimum specific energy consumption during base wine distillation with volume fraction of ethyl alcohol at 10.5 % and brandy distillate production with volume fraction of ethyl alcohol at 70 % is achieved when the tail fraction takeoff begins with ethyl alcohol volume fraction in pairs (alcohol lamp) within the range of 14-16 %. It is demonstrated that production schemes used by various producers to obtain brandy spirits can be optimized, which would increase the output of brandy spirits by 2.4 % and reduce the specific energy costs by 5 %. Optimization of the cognac distillates production scheme does not require additional investment, and can serve as an additional profit source without any equipment upgrade.


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