Decanter Centrifuges

Price range: $49,000.00 through $93,000.00

Decanter centrifuges process characteristics

The separation process in a decanter centrifuge relies on a few process characteristics such as centrifugal force or G-force, sedimentation rate and separating factor, differential speed between the conveyor and bowl, and clarity of the liquid discharge.

Decanter centrifuges require a centrifugal force for the separation of the solids from the liquid.  This characteristic is dependent on the radius of the centrifuge and its angular rotational speed.  A decanter centrifuge applies a force equivalent to several thousand G’s, which reduces the settling time of the particles.  It is also favored to maintain a large G-force, which will result in an improved separation.

The rate at which sedimentation occurs is an important characteristic of the decanter centrifuge separation process.  The sedimentation rate is influenced by the particle size, the shapes of the particles, their differential densities and the viscosity between the particles and the liquid.  This process characteristic can be improved by utilizing flocculating agents.  The sedimentation rate is also dependent on the separating factor of the decanter centrifuge, which is related to the centrifugal force.

The exterior bowl and the scroll conveyor rotate at different high speeds. This differential speed between the two is accountable for the sedimentation throughout the decanter centrifuge cylinder.  A high differential speed results in a smaller residence time of the cake settlement, so it is necessary to keep the cake thickness to a minimum to avoid impairing the discharge quality.  Keeping the cake thickness to a minimum also aids in the improvement of the cake dewatering process.  For this reason, it is necessary to obtain an optimal differential speed to balance the cake thickness and quality.

The characteristic above all affects the clarity of the liquid output which is dependent on the volumetric throughout rate, where a higher flow rate will result in a poor liquid clarity.  Another characteristic that influences the clarity of the liquid output is the differential speed.  A low differential speed results in a better clarity, therefore, aiding in the separation process.  The G-Force also plays a role in the clarity of the liquid discharge.  Higher G-force results in an increase in the separation of the solid particles from the liquid and yields a better clarity.

Description

How does it work

The feed product is pumped into the decanter centrifuges through the inlet. Feed goes into a horizontal bowl, which rotates.  The bowl has is composed of a cylindrical part and a conical part.  The separation takes place in the cylindrical part of the bowl.  The fast rotation generates centrifugal forces up to 4000 x g. Under these forces, the solid particles with higher density are collected and compacted on the wall of the bowl.  A scroll (also screw or screw conveyor) rotates inside the bowl at a slightly different speed.  This speed difference is called the differential speed.  This way the scroll is transporting the settled particles along the cylindrical part of the bowl and up to the end conical part of the bowl.  At the smallest end of the conical part of the bowl, the dewatered solids leave the bowl via discharge opening.  The clarified liquid leaves through a paring disc (internal centripetal pump).

3-phase separation with a decanter

With a 3 phase decanter centrifuge, it is possible to separate 3 phases from each other in one process step only.  For example, two liquids which cannot be mixed because of different densities (e.g. oil and water) are separated from a solids phase.  The heavy liquid (water) collects in the middle between the oil and the solids layer.  Thus the two liquids separated from each other can be drawn off from the decanter.  The solids are transported via the scroll to the discharge openings as it happens also in 2-phase separation.

Typical applications of 3-phase separation are the production of edible oils such as olive oil, oil sludge processing, the production of biodiesel etc.

Parameters and influencing factors of the separation

Feed, throughput and residence time

Through the feed, the separation medium to be processed can be input into the center of the infeed chamber of the scroll, where it is accelerated.  The throughput will have an influence on the residence time.

Decanter Centrifuges Acceleration

The separation medium reaches its maximum speed in the decanter bowl, causing the solids to settle on the bowl inner diameter.  A characteristic feature of the bowl is its cylindrical/conical shape.

Differential speed

There is a differential speed between the decanter bowl and the scroll, which is created by a gear unit on the industrial decanter centrifuges.  The differential speed determines the solid content in the outfeed.

Filling volume / Weir discs or overflow weir

The clarified liquid flows to the cylindrical end of the bowl in the decanter centrifuge, from where it runs out through openings in the bowl cover.  These openings contain precisely adjustable weir discs/weir plates by means of which the pond depth in the bowl can be set.  The weir discs determine the filling volume of the bowl.

 

Advantages and limitations over competitive processes

Generally the decanter centrifuge has more advantages than disadvantages; however, there are some limitations when compared to other processes.

Decanter Centrifuges Advantages:
  • Decanter centrifuges have a clean appearance and have little to no odor problems.
  • Not only is the device easy to install and fast at starting up and shutting down but also only requires a small area for operation compared to other competitive processes.
  • The decanter centrifuge is versatile as different lengths of the cylindrical bowl section and the cone angle can be selected for different applications.  Also, the system can be pre-programmed with various design curves to predict the sludge type, while some competitive processes, such as a belt filter press, cannot change the belt type to operate for different sludge types.  Its versatility allows the machine to have various functions such as operating for thickening or dewatering.
  • The machine can operate with a higher throughput capacity than smaller machines.  This also reduces the number of units required.
  • The device is simple to optimize and operate as it has few major variables and reliable feedback information.
  • The decanter centrifuge has reduced labor costs compared to other processes, as it requires low continuous maintenance and operator attention.
  • Compared to some competitive process such as the belt filter process, the decanter centrifuge has more process flexibility and higher levels of performance.
Decanter Centrifuges Limitations:
  • The decanter centrifuges cannot separate biological solids with very small density differences, such as cells and viruses.  A competitive process that is capable of separating these difficult-to-separate solids is the tubular-bowl centrifuge.
  • The machine can be very noisy and can cause vibration.
  • The device has a high-energy consumption due to high G-forces.
  • The decanter centrifuge has high equipment capital costs. Hard surfacing and abrasion protection materials are required for the scroll to reduce wear and therefore reduce the maintenance of the scroll wear.

Additional information

Weight 2400 lbs
Dimensions 97 × 34 × 54 in
Capacity

1-5 Cu. Ft., 5-20 Cu. Ft., 10-30 Cu. Ft., 32-52 Cu. Ft., 50-80 Cu. Ft.

Voltage

220 VAC, 480 VAC

Manual

PEUSALW300 MANUAL r3

Specifications

You may also like

Flat Filter Centrifuge

Flat Filter Centrifuge

Price range: $13,300.00 through $55,995.00
Select options This product has multiple variants. The options may be chosen on the product page
Translate »
content-1701

yakinjp

yakinjp

rtp yakinjp

yakinjp

yakinjp

yakin jp

yakinjp id

maujp

maujp

maujp

\

sabung ayam online

sabung ayam online

SLOT MAHJONG

sabung ayam online

artikel 000000121

artikel 000000122

artikel 000000123

artikel 000000124

artikel 000000125

artikel 000000126

artikel 000000127

artikel 000000128

artikel 000000129

artikel 000000130

artikel 000000131

artikel 000000132

artikel 000000133

artikel 000000134

artikel 000000135

artikel 000000136

artikel 000000137

artikel 000000138

artikel 000000139

artikel 000000140

artikel 000000141

artikel 000000142

artikel 000000143

artikel 000000144

artikel 000000145

artikel 000000146

artikel 000000147

artikel 000000148

artikel 000000149

artikel 000000150

article 0000091

article 0000092

article 0000093

article 0000094

article 0000095

article 0000096

article 0000097

article 0000098

article 0000099

article 0000100

article 0000101

article 0000102

article 0000103

article 0000104

article 0000105

article 0000106

article 0000107

article 0000108

article 0000109

article 0000110

article 0000111

article 0000112

article 0000113

article 0000114

article 0000115

article 0000116

article 0000117

article 0000118

article 0000119

article 0000120

artikel 0000106

artikel 0000107

artikel 0000108

artikel 0000109

artikel 0000110

artikel 0000111

artikel 0000112

artikel 0000113

artikel 0000114

artikel 0000115

artikel 0000116

artikel 0000117

artikel 0000118

artikel 0000119

artikel 0000120

artikel 0000121

artikel 0000122

artikel 0000123

artikel 0000124

artikel 0000125

artikel 0000126

artikel 0000127

artikel 0000128

artikel 0000129

artikel 0000130

artikel 0000131

artikel 0000132

artikel 0000133

artikel 0000134

artikel 0000135

pengadilan 000086

pengadilan 000087

pengadilan 000088

pengadilan 000089

pengadilan 000090

pengadilan 000091

pengadilan 000092

pengadilan 000093

pengadilan 000094

pengadilan 000095

pengadilan 000096

pengadilan 000097

pengadilan 000098

pengadilan 000099

pengadilan 000100

pengadilan 000101

pengadilan 000102

pengadilan 000103

pengadilan 000104

pengadilan 000105

article 3000061

article 3000062

article 3000063

article 3000064

article 3000065

article 3000066

article 3000067

article 3000068

article 3000069

article 3000070

article 3000071

article 3000072

article 3000073

article 3000074

article 3000075

article 3000076

article 3000077

article 3000078

article 3000079

article 3000080

article 3000081

article 3000082

article 3000083

article 3000084

article 3000085

article 3000086

article 3000087

article 3000088

article 3000089

article 3000090

article 3000091

article 3000092

article 3000093

article 3000094

article 3000095

article 3000096

article 3000097

article 3000098

article 3000099

article 3000100

article 3000101

article 3000102

article 3000103

article 3000104

article 3000105

article 3000106

article 3000107

article 3000108

article 3000109

article 3000110

article 3000111

article 3000112

article 3000113

article 3000114

article 3000115

article 3000116

article 3000117

article 3000118

article 3000119

article 3000120

article 2000081

article 2000082

article 2000083

article 2000084

article 2000085

article 2000086

article 2000087

article 2000088

article 2000089

article 2000090

article 2000091

article 2000092

article 2000093

article 2000094

article 2000095

article 2000096

article 2000097

article 2000098

article 2000099

article 2000100

article 2000101

article 2000102

article 2000103

article 2000104

article 2000105

article 2000106

article 2000107

article 2000108

article 2000109

article 2000110

invoice 00055

invoice 00056

invoice 00057

invoice 00058

invoice 00059

invoice 00060

invoice 00061

invoice 00062

invoice 00063

invoice 00064

invoice 00065

invoice 00066

invoice 00067

invoice 00068

invoice 00069

invoice 00070

invoice 00071

invoice 00072

invoice 00073

invoice 00074

invoice 00075

invoice 00076

invoice 00077

invoice 00078

invoice 00079

invoice 00080

invoice 00081

invoice 00082

invoice 00083

invoice 00084

invoice 00085

invoice 00086

article 238000401

article 238000402

article 238000403

article 238000404

article 238000405

article 238000406

article 238000407

article 238000408

article 238000409

article 238000410

article 238000411

article 238000412

article 238000413

article 238000414

article 238000415

article 238000416

article 238000417

article 238000418

article 238000419

article 238000420

article 238000421

article 238000422

article 238000423

article 238000424

article 238000425

article 238000426

article 238000427

article 238000428

article 238000429

article 238000430

article 238000431

article 238000432

article 238000433

article 238000434

article 238000435

article 238000436

article 238000437

article 238000438

article 238000439

article 238000440

article 238000441

article 238000442

article 238000443

article 238000444

article 238000445

article 238000446

article 238000447

article 238000448

article 238000449

article 238000450

article 238000451

article 238000452

article 238000453

article 238000454

article 238000455

article 238000456

article 238000457

article 238000458

article 238000459

article 238000460

artikel 0000136

artikel 0000137

artikel 0000138

artikel 0000139

artikel 0000140

artikel 0000141

artikel 0000142

artikel 0000143

artikel 0000144

artikel 0000145

content-1701