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MY Nutsche filter
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Introduction:

The MY Nutsche Filter is the industrial version of the well known laboratory scale Buchner Funnel except that it is designed to operate under either on vacuum or pressure. In their modern version they were developed in the early 80's and the majority operates, usually under pressure, in batch oriented industries such as fine chemicals, dyes, pharmaceutics and pesticides.
Present day Nutsche Filters are constructed to perform a multitude of tasks including reaction, filtration, cake washing and thermal drying on a single unit. As such these are very sophisticatedmachines with tight process control on parameters such as pressure, temperature and pH. Nutsche Filters are well suited for handling flammable, toxic, corrosive and odor-noxious materials since they are autoclaved and designed for
MY Nutsche filter

MY Nutsche filter


MY Nutsche filter
(Without dryness)
use in hazardous and ex-proof environments when extremely safe operation is required.
MY Nutsche Filters are available in almost any size with the larger machines for a slurry filling batch of 25 m3 and a cake volume of 10 m3. Such filters have a filtration area of 15 m2 and are suitable for fast filtering slurries that produce readily 0.5 m thick cakes.

Operational Sequence:

The operation of Nutsche Filters requires a complex manipulation of valves and hydraulics so present day installations are always semi or fully automated.
Filtration:
The filter is charged with slurry and pressure is applied to displace the filtrate leaving the cake retained over the filter medium. For slurries with a wide distribution of coarse fast settling solids and slow settling fines there is a risk of segregation with the finer fraction settling over the coarse fraction. When this happens the fines seal the cake and slow down the cake formation so keeping the slurry in suspension with rotating arms during filtration assists in forming a homogeneous cake.
Cake Washing:
In the washing stage a spray ring or connections on top of the cover introduce the wash liquid over the cake. This displaces the mother solution with the wash liquid but with such in-situ washing the efficiency may be quite low if the cake forms with an uneven thickness.
One of the advantages of the Nutsche Filter is the ability to smoothen the cake's surface prior to applying spray wash so that the entire bed is washed evenly.
Washing efficiency may be further improved if air or gas are not allowed to enter the cake in a multi-washing system so the wash liquids always displace the solutions in a "piston" like manner. This is achieved by a special detector that monitors the surface of the cake for moisture and once air or gas start entering the bed a signal is transmitted to close the filtrate valve and reopen it once next washing commences.
Cake Repulping:
Many processes require high washing efficiency to remove the contaminating liquid from the product and washing the cake by repulping yields the most efficient product purity. This is done by resuspending the cake with the paddle arms for thorough mixing with the wash solution. During resuspension the rotating arms are moving slowly downwards and are "shaving" the bed gradually layer after layer until the entire cake enters the slurry.
Pressure Drying:
In the drying stage air or gas purges the cake until the captive moisture is reduced to an asymptotic level and in practical terms the cake is considered to be as dry as possible.
To obtain minimum moisture the cake is smoothened by reversing the rotation of the paddle or auger arms and exerting controlled pressure on its surface with the hydraulic system. This seals cracks in the cake so that air or gas will not bypass the bed.
Cake Discharge:
Once all the stages are completed the cake discharge valve opens and the paddle arms on the smaller machines or the auger arms on the larger ones are rotated and lowered to convey the dry cake towards the center. The same procedure also applies to side discharge machines however it should be noted that in this case the cake comes out intermittently and not continuously. This may have a layout impact on the downstream facility such as the conveyor that handles the product to storage.
On some filters the cloth or woven mesh screen may be backwashed with water to dislodge and remove any cake residue that adhered to the medium after cake discharge.

Feeding and filter ---pulping and washing---pressure drying---cake discharge
-------------------------------------------------------------------------
Feeding and Filter -------- Pulping and Washing -------- Pressure Drying --------- Cake Discharge

Filter's structure:



Filter plate

Filter plate
MY Nutsche filter construction

MY Nutsche filter construction
1.Driving 2.Lifting 3.Washing
4.Top vessel 5.paddle arms 6. discharge valve
7.Filter plate 8.Bottom vesse l9.Frame
a.Feed inlet b.Washing inlet c.Pressure air inlet
d.Filtrate outlet e.Cake discharge outlet

Technical parameters:


Model
MY600-N
MY800-N
MY1000-N
MY1200-N
MY1400-N
MY1600-N
MY2000-N
MY2400-N
MY2800-N
Vessel Diameter (mm)
600
800
1000
1200
1400
1600
2000
2400
2800
Filtration Area (m2)
0.25
0.5
0.75
1.0
1.5
2.0
3.0
4.5
6.0
MAX Slurry Volume (m3)
0.2
0.48
0.8
1.0
1.6
2.4
4.5
6.0
6.0
MAX Cake Height (mm)
200
250
250
300
400
400
500
500
500
Motor Power (kW)
2.2
4
4
5.5
7.5
11
15
18.5
22
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Company Address:No.29,TianHu Road,New&High Technology Park,west Changjiang road,HeFei city,AnHui Provice,China (Postcode:230088)
Tel:(0086)0551-5310098 5311098 Fax:(0086)0551-5311098