SU700541A1

SU700541A1 - Mixer-winfier

Info

Publication number: SU700541A1
Application number: SU782626325A
Authority: SU
Inventors: Анатолий Владимирович Иваненко; Сергей Васильевич Касько; Константин Федорович Бодян; Дмитрий Александрович Моисеенко; Михаил Кузьмич Мордвинов; Анатолий Агзамович Галиулин
Original assignee: Одесский Технологический Институт Пищевой Промышленности Им. М.В.Ломоносова
Priority date: 1978-06-08
Filing date: 1978-06-08
Publication date: 1979-12-05

Description

Изобретени относитс к пищевой промышленности , винодельческой ее отрасли, а именно к смесител м-винификаторам.The invention relates to the food industry, its wine industry, namely, the mixer m-winemakers.

Известен смеситель-вш-шфикатор, состо щий из цилиндрического резервуара с патрубками и фильтрующей перегородкой 1.A mixing mixer is known, consisting of a cylindrical tank with nozzles and a filter partition 1.

Недостатком известного смесител -винификатора вл етс низка интенсивность нроцессов экстракции, диффузии и тепломассообмена.A disadvantage of the known mixer-converter is the low intensity of the processes of extraction, diffusion and heat and mass transfer.

Цель изобретени - инте {сифика1и процессов экстрак1ши, диффузии и тепломассообмена.The purpose of the invention is to entertain the processes of extraction, diffusion and heat and mass transfer.

Указанна цель достигаетс тем, что смеситель-випификатор снабжен кривошипно-щатунным механизмом, соединенным через нггок с фильтрующей перегородкой, а патрубки выполнены так, что их оси на участках соединени с цилиндрическим резервуаром образуют с поверхностью перфорированной перегородки . угол 30-60°.This goal is achieved by the fact that the mixer-vipifikator is equipped with a crank-paddle mechanism connected via a filter to the filter septum, and the nozzles are designed so that their axes in the junction areas with the cylindrical tank are formed with the perforated septum surface. angle of 30-60 °.

При :JTOM кривоишпно-шатунный механизм снабжен винтом дп перемещени кривошипа и электродвигателем, а шток выполнен телес; :о1шческим .When: JTOM crank mechanism is equipped with a screw for moving the crank and an electric motor, and the rod is made of a body; : about 1

На фиг. 1 представлен смеситель-винификатор , в разрезе; на фиг. 2 -- разрез А-А на фиг. 1.FIG. 1 shows the mixer-vinifikator, in section; in fig. 2 shows section A-A in FIG. one.

Смеситель-винификатор состоит из фасонного резервзара 1. снабженного патрубками 2 и 3 Ц11 входа и выхода первого потока, патрубками 4 и 5 дл входа и выхода второго потока.The vinifier mixer consists of a shaped back-up 1. equipped with nozzles 2 and 3 TS11 of the first stream inlet and outlet, branch pipes 4 and 5 for the inlet and outlet of the second stream.

В резервуаре 1 расположена параллельно движению потоков фильтрующа перфорированна перегородка 6, приводима в возвратно-поступательное движение в цилиндрической части резервуара 7 штоком 8. Резервуар 1 имеет фасонные приливы 9, создаюпдае направленные перемещени потоков под углом Ос к подвижной перфорированной перегородке, равным 30-60°. Шток 8 имеет (елескопическую часть 10 и контргайку II.In the tank 1, the perforated filter partition 6 is parallel to the flow movement, driven in reciprocating motion in the cylindrical part of the tank 7 by the rod 8. The tank 1 has shaped tides 9, creating directional movements of the flows at an angle Oc to the movable perforated partition equal to 30-60 ° . The rod 8 has a (Elescopic part 10 and a locknut II.

Claims

The movement of the rod is transmitted or crank mechanism 12, crankshaft 13 which has the potential to move radially with the screw 14. The rotation of the crank mechanism by the motor 15 with the controlled frequency x of the torus. Mixer-vinifikator works as follows. The perforated overflow filter 6 performs an oscillatory movement perpendicular to the direction of the cold and heat-treated pulp flows. The hole diameter of the perforated septum is 3.5-4.0 mm, which is 0.7-0.9 of the average seed diameter of the pulp and therefore the solid parts of the pulp do not pass through it, and the wort is squeezed through: the holes and carried away by adjacent streams . When the septum 6 moves, pressure oscillations and overflowing jets of the tour occur (5 lyse currents, which intensifies the diffusion processes of the extracted substances into the mash. Inertial forces, as well as counter flows, jet streams the solid parts of the pulp from the partition 6 and they are carried away from the tank 1 by pulp flows This also contributes to the design of the mixer-casing housing, since the axes of the pipes 2, 3, 4, 5 entering the cylindrical part of the tank 1 are at an angle of 30-60 ° to the surface of the filter septum, with In this case, the pulp flows wash it, preventing the hole from clogging. By varying the oscillation frequency of the partition 6 with the help of a controlled electric motor 15, as well as the amplitude of its movement, the adjustment of the radius of the curvature 13 controls the magnitude of the heat and mass transfer. The partitions 6 inside the tank 1, with the help of the telescopic part 10 of the shaft 8, cause a change in the amount of fluid passing through the partition from adjacent streams. The design of the proposed mixer-vinifier allows to intensify the processes of extraction, diffusion and heat and mass transfer. Claim 1. A mixer wikifikator consisting of a ciliridric tank with nozzles and a perforated partition, characterized in that, in order to intensify the processes of extraction, diffusion and heat exchange, it is equipped with a crank mechanism connected to a filter with a partition and made so that their axes in the areas of connection with the cylindrical tank form an angle of 30-60 ° with the surface of the perforated partition.

2. The vinifier mixer according to claim 1, which is different in that the crank-rod mechanism is equipped with a screw for moving the crank and motor, and the shaft is made telescopic. Sources of information taken into account during the examination 1. USSR author's certificate N 589001, cl. C 12 G 1/02, 1976.