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6-S shaker belongs to gravity beneficiation equipment, developed from the plane chute, characterized by its asymmetric reciprocating motion and its own system. Suitable for sorting 2-0.037 mm ore and slime grade gold, tungsten, tin, tantalum, iron,manganese, chromium, titanium, bismuth, lead and other nonferrous, black, rare and   precious metal minerals, sorting 4-0.037 mm pyrite; After changing the form of the bed bar properly, it can select the non-metal such as coal and coal slime, monazite, rutile, and other mixed materials with enough specific gravity difference and particle size composition.

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    제품 개요

    The beneficiation process of the shaker is carried out on the inclined bed surface with repeated strips. The ore particles are sent from the feed trough at the corner of the bed surface, and the transverse washing water is supplied to the feed trough. Under the action of gravity, the transverse water impulse, the inertia and friction caused by the    reciprocating asymmetric movement of the bed surface, the ore particles are stratified according to specific gravity and particle size. The longitudinal motion along the bed   surface and the transverse motion along the inclined bed surface are made. Therefore, the ore particles with different specific gravity and particle size gradually fan down in   their respective direction of movement, respectively from different areas of theconcentrate end and tailings side, and finally are divided into concentrate, ore and tailings.The outstanding advantage of 6-S shaker is that the separation accuracy is high, and the final concentrate, middle ore and waste tailings can be obtained after a single separation, and multiple products can be obtained at the same time. The concentration ratio of concentrate is high, the sorting efficiency is high, the care is easy, and the stroke is easy to adjust.


    작업 원리

    Shaker sorting is realized under the joint action of bed shaking and transverse   water flow. Bed bed strips are longitudinal and the direction of water flow is close to vertical. When water flow crosses each bed strip laterally, eddy currents are formed in the groove. The combined action of eddy currents and bed shaking can loosen the mineral sand layer and stratify it according to density. The upper light ore particles are subject to the greater impulse of the water flow, while the lower heavy ore particles are subject to the lesser impulse, so the transverse movement speed of the light ore particles on the bed is greater than that of the heavy ore particles on the bed. This process is called "de lamination".

    세로 방향으로, 침대 표면의 차등 운동은 처음에는 느린 속도로, 점차적으로 가속화되고, 갑작스런 후퇴가 후퇴 과정에서 속도가 점차 감소한 다음, 위의 과정을 반복하고, 위의 과정을 반복하고, 광석 층의 느슨한 계층화를 촉진 할뿐만 아니라, 더 큰 속도를 향하여 전진하여 전진하여 전진하여, 더 큰 경착 전속을 전진 시켜서, 더 큰 포지티브를 앞으로 나아가게한다. 광석 입자가 이동하는 곳은 종 방향 속도와 가로 속도의 조합에 달려 있습니다. 중형 미네랄은 가로 속도가 작고 더 큰 종 방향 속도를 가지며, 광물 미네랄은 가로 속도가 더 크고 세로 속도가 작습니다.

    Applying the parallelogram rule to synthesize the longitudinal velocity and transverse velocity, it can be seen that the combined velocity of heavy minerals is inclined to the concentrate end of the shaker, light minerals are inclined to the tailings side of the shaker, and medium density particles are located between the two. This process is called "transport banding".Since the height of the bed is gradually reduced along the longitudinal direction of the self-driving end, the stratified ore particle groups in the groove are continuously stripped off during the movement to the concentrate end. 

    그루브의 상부 층의 광물이 먼저 벗겨져 층 표면의 수평 방향을 따라 광미쪽으로 이동하고, 무거운 미네랄은 농축액 끝에서 배출됩니다. 따라서, 전체 층 표면의 미네랄은 다양한 중력과 다른 입자 크기에 따라 팬 분포를 나타내므로 다양한 제품을 얻습니다.

    The concentrate strip is washed by transverse water flow in the smooth area of  the bed surface (no bed strip area), so that a few gangue particles mixed in it are washed out, and the grade of the concentrate is further improved.


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