JP2006340638A - Successive dewatering apparatus and successive dewatering method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To reduce the contained water as possible by dewatering seaweeds at high efficiency. <P>SOLUTION: The successive dewatering apparatus is obtained as follows. A dewatering vessel having a bottom is installed in the inside of an outer vessel so as to be freely rotated, and a screw cylinder comprising a screw belt having a brush fixed on the outside is installed in the inside of the dewatering vessel so that the outside may approach the inner wall of the dewatering vessel. The dewatering vessel and the screw cylinder are arranged so that a material to be dewatered may be moved from a lower part to an upper part by the difference of rotational speeds. A draining port is installed in the lower part of the outer vessel, and a cylinder for discharging the dewatered material is installed so as to be connected to the upper part of the dewatering vessel. A power is connected to the dewatering vessel and the screw belt. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a continuous dehydration apparatus for reducing the moisture contained in fresh seaweed, kombu, seaweed, blue seaweed and the like as much as possible, and facilitating drying treatment after drought, and continuous dehydration using the same. Regarding the method.

  Conventionally, rotating and rotating a spiral rotating brush into a separation cylinder having a large number of minute holes on the peripheral wall to separate the water and the water is usually employed in a raw laver treatment line.

Further, the whole fruit of citrus fruits is supplied between the screen filter body and the spiral member, and the screen filter body and the spiral member are rotated to obtain juice, and the separated residue is taken out by the spiral member. A squeezing device is known.
Shoko 61-44632 JP 55-64789

  According to the conventional raw seaweed dehydrator (for example, Japanese Utility Model Publication No. 61-44632), the dehydration is relatively small (for example, 300 rpm) and has a small diameter (for example, 200 mm to 300 mm). For this reason, centrifugal force was small and dehydration was insufficient.

  The washing dehydrator was intended to remove foreign substances and generally dehydrated, so it was not necessary to reduce the water content (for example, 50% or less) (this was an intermediate process of raw seaweed treatment).

  Further, in the juice squeezing device, only the juice should be separated, and the peels and other solids were relatively large, so there was little risk of clogging. However, in a dehydrating apparatus for significantly reducing moisture (for example, moisture of 30% or less), it is necessary to increase the centrifugal force sufficiently. Therefore, the rotational speed is set to 1000 rpm or the diameter of the dehydrating tank is set to 500 mm or more. Without such treatment, there was a problem that continuous high-efficiency dehydration was impossible.

  Also, when dewatering seaweeds such as fresh seaweed, seaweed, blue seaweed, and kombu, fine pieces are mixed in and there are wide areas that often block the inner wall of the dehydration tank. There was a problem that there was.

  In high-speed continuous dewatering, it is necessary to continuously remove dehydrated material (for example, dehydrated raw laver). However, brush dehydration that has been used in the past requires smooth removal of raw laver by attaching to the brush. There was a problem that could not be.

  In this invention, a spiral cylinder is installed in a dewatering tank, both are rotated at a high speed with a slight rotational difference, and a brush is fixed to the back surface of the outer edge of the spiral band constituting the spiral cylinder, and the tip of the brush is attached. By sliding the inner wall of the dewatering tank, clogging is prevented and smooth transfer of the dehydrated material is ensured, thereby solving the conventional problems.

  That is, the present invention is a spiral in which a bottomed dewatering tank is rotatably built inside the outer tank, the inner side of the dewatering tank is placed close to the inner wall of the dewatering tank, and a brush is fixed to the outer edge. A spiral cylinder made of a belt is rotatably laid, the dehydration tank and the spiral cylinder can move the dehydrated material from below to above due to a rotational speed difference, a drain port is provided at the lower part of the outer tank, A continuous dewatering device characterized in that a dehydration discharge tube is connected to the upper part of the dewatering tank, and the power is connected to the dewatering tank and a spiral band. A plurality of support columns for supporting the spiral band on the periphery are installed on a concentric circumference, and the band body is spirally fixed to the outside of the support column, and the inner wall of the dehydration tank is connected to the outer edge of the band body. A brush with a length that is in sliding contact with is fixed.

  A combination of the dehydrating apparatus according to claim 1 and a dehydrating apparatus according to claim 1, wherein a dehydrating cylinder is installed in the outer tub and a brush cylinder in which a brush is helically installed in the dehydrating cylinder is rotatably installed. The dehydration tank and the spiral cylinder are configured to adjust the moving speed of the dehydrated material upwards or downwards depending on the difference in the number of rotations of the spiral cylinder. It was installed in.

  In another invention, a rotating spiral cylinder is installed in a rotating dewatering tank, and the tip brush of the spiral band is brought into sliding contact with the inner wall of the dehydrating tank to prevent clogging and cleaning. The dewatered material supplied into the lower part of the dewatering tank is moved upward, and the dewatered material supplied between the dewatering tank and the spiral cylinder is continuously dehydrated. In the separation cylinder, the material to be dehydrated is subjected to brush dewatering by rotating a spiral brush, and then supplied to the dewatering tank for continuous dewatering.

  In the present invention, fresh seaweed, blue seaweed, seaweed, and kombu are collected and dried. Traditionally, seaweed and kombu have been sun-dried for a long time, but the production was difficult due to the weather. In addition, fresh seaweed, blue seaweed, seaweed, and kombu are preferable for mechanical dehydration because of their poor drying efficiency. However, due to the characteristics of seaweed, it is necessary to increase the centrifugal force in centrifugal dehydration. When the centrifugal force is increased, efficient removal is difficult.

  Also, since seaweed is wide, even if it is cut in the length and width directions, it still has a width of 30 to 50 mm and closes the water passage hole of the dehydration tank, but there is no way to solve this effectively. . Therefore, a spiral band was used for transfer, and a brush was used for clogging (utilizing the characteristics of both).

  In the said invention, although rotation of a dehydration tank changes with diameters, if it is 600 mm-1000 rpm with a diameter of 500 mm, the isolation | separation water | moisture content (adhesion water | moisture content) of fresh laver will be dehydrated to 30% or less. Therefore, drying after dripping (water 5% to 10% intracellular water) becomes very easy.

  In the case of fresh seaweed, even if pumped from a storage tank (stirring tank) and directly applied to a continuous dehydrator, the dehydration efficiency is poor due to excessive water (for example, water of 50% or more). It is preferable to subject the dehydrated product to a continuous dehydration treatment.

  The above has mainly described the dehydration of fresh seaweed, but the same is true for blue seaweed, seaweed, and kombu. In this case, it is more efficient to perform rough cutting (for example, cutting a length of 100 mm to 300 mm into 50 mm to 100 mm).

  Next, the rotation difference between the dewatering tank and the spiral cylinder is set to 3 to 5 rotations so that the dehydrated material at the bottom of the dewatering tank is sequentially taken out in about 30 seconds. This time is determined by the difference between the rotational speeds of the dewatering tank and the spiral cylinder and the pitch of the spiral band.

  In the spiral cylinder of the invention, a strip plate (for example, stainless steel tape) is spirally installed on the outer wall of the cylindrical body, and several columns are concentrically arranged to spiral the strip plate to this column. In some cases, it may be arranged to form a spiral band, but the main point is to carry the dehydrated material upward, and therefore, a material and a structure that can achieve this purpose are preferable.

  The material of the spiral band is preferably a metal band (for example, stainless steel tape) that does not rust in terms of handling seaweed (or salt water), but may be a synthetic resin band.

  Further, the brush is fixed to the lower surface of the outer edge portion of the spiral band, and its tip has a length that allows sliding contact with the inner wall of the dewatering tank. Although it may be attached to the upper surface of the spiral band, it is considered that the lower surface is preferable in consideration of attachment of fresh seaweed or the like.

  Since the length of the brush is such that the tip is in sliding contact with the inner wall of the dewatering tank, it naturally protrudes from the outer edge of the spiral band.

  The brush in the above is made of synthetic resin fiber, has elasticity, and is continuously fixed to the back surface of the spiral band with a bundle of several to several tens.

  According to the present invention, the dehydration tank and the spiral cylinder are respectively rotated, and the difference in rotational speed between the two is made so that the dehydrated matter is taken out. However, there is an effect that the dehydrated product can be taken out through sufficient dehydration treatment. In addition, there is an effect that the take-out speed can be adjusted by the difference in rotational speed between the dehydrating tank and the spiral cylinder.

  In addition, the combined use of brush dehydration and continuous dehydration has the effect of reproducing a high dehydration rate that could not be achieved previously.

  In this invention, raw nori with a water content of 70% or more, which has been washed and dewatered by roughly cutting raw nori and applying it to a brush dehydrator, is sequentially placed in a dehydration tank having a diameter of 600 mm and a height of 400 mm, and is rotationally dehydrated at 1000 rpm. As a result, raw nori with a moisture content of 20% to 30% was produced. This raw nori was dried at 50 ° C. for 2 hours, and a dry nori for processing having a moisture content of 5% was obtained.

  An embodiment of the present invention will be described with reference to the drawings. An outer tub 2 is installed on a machine base 1, and a dehydrating tub 3 is installed concentrically and rotatably in the outer tub 2 at a predetermined interval. To do. The dewatering tank 3 fixes a bottom plate 5 to a lower end portion of a cylinder 4 in which a metal plate having a large number of minute holes (for example, a diameter of 0.3 mm) is formed in a cylindrical shape, and a reinforcing ring 6 to an outer wall of the cylinder 4. , 6 are fixed up and down at predetermined intervals. The upper end of the tube shaft 7 is connected to the lower center of the bottom plate 5. A spiral cylinder 8 is installed concentrically on the inside of the dehydration tank 3 so as to be rotatable.

  The spiral cylinder 8 has a circular bottom plate 10 fixed to the upper end of a rotating shaft 9 inserted through the tube shaft 7, and equal-length columns 11, 11 (for example, eight) are fixed upright at equal intervals to the peripheral edge of the circular bottom plate 10. The circular top plate 10a is fixed to the upper ends of the columns 11, 11, and the stainless steel strip 12 is helically fixed to the outside of the columns 11, 11 to form the spiral cylinder 8. A synthetic resin fiber bundle is fixed to the stainless steel strip 12 on the lower surface of the outer edge portion closely or at a predetermined interval to form a brush 13. The brush 13 is for preventing clogging of the dewatering tank 3 and has a length that is in sliding contact with the inner wall of the dewatering tank 3.

  A feeding cylinder 14 is installed at the center of the spiral cylinder 8, and a dehydration take-out cylinder 15 is connected to the upper side of the outer tank 2 obliquely downward. A drain tube 16 is continuously provided on the side.

  In the above, when the dehydrated material is raised by the stainless steel belt fixed to the spiral shape of the spiral cylinder 8 and reaches the uppermost part, it is placed on the plate 47 that closes the gap between the dehydration tank 3 and the upper part of the outer tank. Although rising, air rises along the inner wall of the dewatering tank and is discharged to the outside through the take-out cylinder 15, so that dehydrated matter is also taken out by this wind force. In the above, when the dehydrating cylinder rotates at 600 rpm to 1000 rpm, the air rising from below to the upper part also flows very quickly (for example, 1 m / sec), and the suspended matter in the middle is blown away and taken out. Therefore, it is not necessary to forcibly discharge the dehydrated material with a rotating blade or the like.

  Further, an outer tub 18 is installed on the machine body 17, separation cylinders 19 are installed in the outer tub 18 at predetermined intervals, and a brush cylinder 20 is concentrically and rotatably installed in the separation cylinder 19. In the brush cylinder 20, a brush strip is formed on the outer wall of the cylinder 21 in a spiral manner to form a brush strip 22, and the outer end of the brush strip 22 is in sliding contact with the inner wall of the separation cylinder 19.

  At the top of the outer tub 18, there is provided a take-out trough 23, and at the bottom is a drain trough 24, and one end of a hose 25 is connected to the inside of the bottom of the separation cylinder 19. The end is connected to the discharge port of the cutter 26.

  In the above-described embodiment, when the original algae are fed from the inlet tube 27 of FIG. 1 as indicated by an arrow 28, the original algae are cut into 50 to 100 mm by the cutter 26, and the hose 25 is indicated by the arrow 29. And is fed into the lower part of the separation cylinder 19.

  Therefore, when the brush cylinder 20 is rotated (for example, 300 rpm), the raw seaweed is washed while rising as indicated by an arrow 30, and the minute foreign matter and water pass through the separation cylinder 19 and are outer tanks as indicated by an arrow 31. It enters 18 and is discharged from its lower part.

  The washed raw seaweed is lifted by the brush strip 22, taken out from the take-out basket 23 as indicated by an arrow 32, and supplied into the input cylinder 14 as indicated by an arrow 33.

  The raw laver thrown into the throwing cylinder 14 falls as indicated by an arrow 34 and is received on the circular bottom plate 10, but the circular bottom plate 10 is rotated at a high speed (for example, 1000 rpm), so that it is powerful. Under the centrifugal force, it is splashed in the horizontal direction as shown by arrow 35, hits the cylinder 4 of the dewatering tank 3, the water accumulates in the outer tank 2 as shown by arrow 36, and the raw laver is guided to the spiral zone. Then, it rises along the inner wall of the cylinder 4 as indicated by arrow 37, is collected on the upper side, and is taken out from the take-out cylinder 15 to the outside as indicated by arrow 38. On the other hand, the drainage is collected in the lower part of the outer tank and drained from the drain tube 16 as indicated by an arrow 39.

  The rotary tube shaft 7 is attached to a case of the speed reducer 44, and is rotated by a motor 43 through a pulley 40, a V belt 41, and a pulley 42 attached to the case of the speed reducer 44.

  The rotary shaft 9 is connected to the output shaft 45 of the speed reducer 44 and rotates at a rotational speed (reduction ratio of the speed reducer 44) smaller than the rotational speed of the case of the speed reducer 44.

  Accordingly, the dehydration take-out speed can be determined by the rotation speed of the motor 43 and the reduction ratio of the reduction gear 44.

  The input shaft 46 of the speed reducer 44 is fixed in order to generate a negative rotation of the rotary shaft 9.

  According to the embodiment, the dewatering efficiency can be determined mainly by the rotation speed of the dewatering tank. Moreover, if the rotation difference between the dehydration tank and the spiral cylinder is adjusted, the residence time of the raw laver is determined, and the dehydration rate can be adjusted accordingly. In the above embodiment, continuous dewatering is performed after brush dewatering. However, brush dewatering may be omitted to perform continuous dewatering.

  An embodiment of the method according to the present invention will be described with reference to FIG. 2. The raw algae and water (seawater) are mixed in equal amounts or with an increased amount of water and fed by a pump (50 liters per minute).

  Next, it is cut into a length of 50 to 100 mm with a cutter and brush dehydrated. In this case, the fine foreign matter is removed together with the waste water by washing. In this case, the moisture after draining is 70% or more.

  Next, centrifugal dehydration is performed at 1000 rpm to obtain raw nori with a moisture content of 20% to 30%. This raw seaweed is used for processing, for example, dried to a moisture of 10% or less, crushed and used for sprinkling.

  Conventionally, it took a lot of time, heat, and labor to dry from about 50% moisture to 10% or less, but the dehydration of the present invention reduced the heat of drying to 30% and saved labor and time. It was.

Explanatory drawing which cut | disconnected a part of Example of this invention. (A) The partial top view which cut the same partially, (b) The partial cross-section enlarged view which similarly shows the brush attachment state. Similarly block diagram.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Machine stand 2 Outer tank 3 Dehydration tank 4 Cylinder 5 Bottom plate 6 Reinforcement ring 7 Rotating tube shaft 8 Spiral tube 9 Rotating shaft 10 Circular bottom plate 11 Support column 12 Circular top plate 13 Brush 14 Input tube 15 Extraction tube 16 Drain tube 17 Machine body 18 Outer tank DESCRIPTION OF SYMBOLS 19 Separation cylinder 20 Brush cylinder 21 Cylinder 22 Brush strip 23 Extraction rod 24 Drainage rod 25 Hose 26 Cutting device 40 Pulley 41 V belt 42 Pulley 43 Motor 44 Reduction gear 45 Output shaft of reduction gear 46 Input shaft of reduction gear

Claims (7)

  A spiral cylinder comprising a spiral band in which a bottomed dewatering tank is rotatably installed inside the outer tank, the inner side of the dewatering tank is positioned close to the inner wall of the dewatering tank, and a brush is fixed to the outer edge. The dehydrating tub and the spiral cylinder are configured to be rotatable, so that the dehydrated material can be transferred from the lower side to the upper side due to a difference in rotational speed, and a drain port is provided at the lower part of the outer tank, and the upper part of the dehydrating tank is provided. A continuous dewatering apparatus, wherein a dewatered material discharge cylinder is connected in series, and power is connected to the dewatering tank and a spiral belt.   A plurality of pillars for supporting the spiral band on the outer peripheral edge of the circular top plate and the circular bottom plate opposed to each other are installed on a concentric circumference, and the belt body is spirally fixed to the outside of the pillar, and The continuous dewatering device according to claim 1, wherein a brush having a length that is in sliding contact with an inner wall of the dewatering tank is fixed to an outer edge portion of the belt body.   2. A brush dehydrating apparatus in which a dehydrating cylinder is installed in the outer tub and a brush cylinder in which a brush is spirally installed in the dehydrating cylinder is rotatably installed, and the dehydrating apparatus according to claim 1 is combined. A continuous dehydrator.   2. The continuous dehydration apparatus according to claim 1, wherein the dehydration product is configured to adjust the moving speed of the dehydrated product upward and downward depending on the difference in rotational speed between the dehydration tank and the spiral cylinder.   The continuous dehydration apparatus according to claim 1, wherein the spiral cylinder has a spiral band spirally installed on the outer wall of the cylinder.   A rotating spiral cylinder is installed in the rotating dehydration tank, and the spiral brush is in sliding contact with the inner wall of the dehydration tank to prevent clogging and cleaning. A continuous dehydration method characterized in that the dehydrated product supplied to the water is moved upward, and the dehydrated product supplied between the dewatering tank and the spiral cylinder is continuously dehydrated.   The continuous dehydration method according to claim 6, wherein the material to be dehydrated is supplied to the dewatering tank and continuously dehydrated after brush dewatering by rotating a spiral brush in the separation cylinder.

Images