Polymer Plant Eqpt 1

133

Transcript of Polymer Plant Eqpt 1

Page 1: Polymer Plant Eqpt 1
Page 2: Polymer Plant Eqpt 1

POLYMER PLANT EQUIPMENT

Equipment handled by PED in a typical Polymer Plant

CentrifugeRotary dryerPneumatic Conveying SystemMetering PackageMixers (Homogeniser)Extruder & PelletiserDelumper Dewatering ScreenPellet DryerClassifier ScreenBagging & Palletising Systems

Page 3: Polymer Plant Eqpt 1

POLYMER PLANT EQUIPMENTREACTOR CENTRIFUG

EROTARY DRYER

POLYMER POWDER STORAGE

METERING PACKAGE

HOMOGENISER MIXER

EXTRUSION & PELLETISING

PELLET STORAGE

BAGGING & PALLETISING

ETHYLENEH2

SOLVENTCATALYST

SOLVENT (LIQ.)

POLYMER CAKE

POLYMER SLURRY

SOLVENT (VAP.)

ADDITIVESSTABILIZERS

DEWATERING

SPIN DRYING

CLASSIFICATION

BLENDING

ELUTRIATION / SCREENING

BAGGING STORAGE

WAREHOUSING

Page 4: Polymer Plant Eqpt 1

CENTRIFUGEPurpose:To separate polymer solids from polymer slurry

Working PrincipleThe basic centrifuge idea is based on what happens in a settling tank, in which particles, sediment and solids gradually fall to the bottom, and the liquid phases of different density separate due to the force of gravity. However, such clarification is an extremely slow process and is unable to meet industry's needs for rapid, controllable results. The general idea behind centrifuges is therefore to ensure that the mechanical separation of different liquid phases and solids can be carried out on a rapid, continuous basis in order to meet the demands associated with modern industrial processes.

Page 5: Polymer Plant Eqpt 1

In essence, a centrifuge is a settling tank whose base is wrapped around a centerline.Rotating this entire unit rapidly means that the effect of gravity is replaced by a controllable centrifugal force that can have an effect upto 10,000 times greater.This force is then used to separate liquids from other liquids or solids.

Page 6: Polymer Plant Eqpt 1

SETTLING TANK SETTLING TANK WITH DISCS

DISC STACK CENTRIFUGE

Page 7: Polymer Plant Eqpt 1

CENTRIFUGETypes:

• Horizontal • Vertical• Atmospheric • Pressurised• Solid Bowl • Screen Bowl

Page 8: Polymer Plant Eqpt 1

CENTRIFUGE Decanter centrifuges are generally used for

greater solids concentrations with larger particle sizes.

Disc stack centrifuges, on the other hand, are ideal for a wide range of separation tasks that involve lower solids concentrations and smaller particle and droplet sizes. This applies to both liquid liquid and liquid solid separation.

Page 9: Polymer Plant Eqpt 1

CENTRIFUGE

Filters

Disc Stack Centrifuges

Decanter Centrifuges

Particle Size(µm)

Amount of Solids

40%

30%

20%

10%

0.1 1 10 100 1000

Page 10: Polymer Plant Eqpt 1

Disc Stack Vertical Centrifuge

Inserting special plates (the "disc stack") provides additional surface settling area, which contributes tospeeding up the separation process dramatically. It is the particular configuration, shape and design ofthese plates that make it possible for a disc stack centrifuge to undertake the continuous separation of a wide range of different solids from either one ortwo liquids.

Page 11: Polymer Plant Eqpt 1

The concentrated solids phase formed by the particles can be removed continuously, intermittently or manually, depending on centrifuge type and the amount of solids involved in the specific application.The clarified liquid phase (or phases) overflow close to the rotating axis, in the outlet area on top of the bowl. The liquids then flow into separate chambers. Each separated liquid phase then leaves the bowl due to the force of gravity or by means of a paring disc, which is a special pumping device. The chambers can be sealed off from each other to prevent any riskof cross-contamination.

Page 12: Polymer Plant Eqpt 1

How a disc stack centrifuge works ?

A disc stack centrifuge separates solids and one or two liquid phases from each other in one single continuous process, using extremely high centrifugal forces. When the denser solids are subjected to such forces, they are forced outwards against the rotating bowl wall, while the less dense liquid phases form concentric inner layers.The area where these two different liquid phases meet is called the interface position. This can be easily varied in order to ensure that the separation takes place with maximum efficiency.

Page 13: Polymer Plant Eqpt 1

CENTRIFUGE

Solid Retention Intermittent Solid Discharge

Continuous Solid Discharge

Page 14: Polymer Plant Eqpt 1

CENTRIFUGE (BOWL TYPE)The separated solids are conveyed by the helical screw conveyor along the bowl cylinder and over the conical section of the decanter to the solids discharge. As they pass over the cone, the solids dewater by a combination of drainage and compression, the degree of which is dependent on the nature of the solids, the adjustment of the centrifuge, and the required degree of dewatering.

Page 15: Polymer Plant Eqpt 1

CENTRIFUGE(SOLID BOWL)

Page 16: Polymer Plant Eqpt 1

CENTRIFUGE(SCREEN BOWL)

 Actually two machines in one combines the clarifying benefits of the solid bowl centrifuge and adds a final dewatering screen section to produce maximum dryness. Best suited for crystalline or granular solids  with free-draining characteristics. Unit capacities up to 100 tons/hr dry solids.

Page 17: Polymer Plant Eqpt 1

CENTRIFUGE(SCREEN BOWL)

Page 18: Polymer Plant Eqpt 1

CENTRIFUGE(VERTICAL)

Page 19: Polymer Plant Eqpt 1

POLYMER DRYERSThe wet slurry out of Centrifuge still has about 30% solvent / water. This needs to be dried in Dryer.

Types of Dryers:

Rotary Dryers Fluidised Bed Dryers

Page 20: Polymer Plant Eqpt 1

ROTARY DRYERType Of Rotary Dryers

Direct Fired TypeSteam Tube Type

Page 21: Polymer Plant Eqpt 1

ROTARY DRYER (DIRECT FIRED TYPE)

Operating Principle

In direct fired dryers, hot air generated by firing of fuel is made to pass through rotating drum with lifters. Hot air when comes in contact with the wet slurry, dries the polymer powder which is conveyed either pneumatically or through rotating scroll

Page 22: Polymer Plant Eqpt 1

ROTARY DRYER(STEAM TUBE TYPE)

This unit gives continuous heating or cooling of solids in an inert atmosphere, or in a medium vacuum state or under pressure. Indirect heat transfer is effected by conduction and convection, and constant temperature can be set by steam pressure. Unit operation is closed. Complete recovery is possible. Low sweeping gas required.

Page 23: Polymer Plant Eqpt 1

ROTARY DRYER(STEAM TUBE TYPE)

The wet feed which has free flowing granular form is made to work over the rotating bundle of heated tubes.

Due to radiation and conduction effects, the moisture is evaporated and the product becomes

progressively dry as it travels across the dryer and reaches final

moisture level at the discharge point.

Due to effective turbulence the solids are dried uniformly.

Page 24: Polymer Plant Eqpt 1

ROTARY DRYER

Page 25: Polymer Plant Eqpt 1

ROTARY DRYER

Page 26: Polymer Plant Eqpt 1

ROTARY DRYER (TYPICAL P&ID)

Page 27: Polymer Plant Eqpt 1

FLUIDISED BED DRYERSMaterials are treated in fluidized, agitated and suspended conditions by various gases. Heat is provided directly by burning fuel or injecting fuel to the fluid bed.

Heating elements for indirect heating by steam can also be installed.

Spent off-gas can be recycled for preheating air to save fuel Spent off-gas can be recycled for preheating air to save fuel costs. This is a relatively maintenance-free equipment.costs. This is a relatively maintenance-free equipment.

Page 28: Polymer Plant Eqpt 1

METERING SYSTEMSMetering Systems are required for feeding of controlled and metered quantities of virgin Polymer Powder and other additives to impart the required properties to the end product.

Types of Metering Feeders:

Volumetric Feeders Gravimetric Feeders Mass Flow Meters Belt Feeders

Page 29: Polymer Plant Eqpt 1

Typical Compounding in Polymer Plant

Loss in Weight Feeders

Page 30: Polymer Plant Eqpt 1

Loss in Weight Feeder

Loss in Weight FeedersMass Flow Feeder

Page 31: Polymer Plant Eqpt 1

How Loss in Weight Feeders work?

The Feeder and the supply bin are weighed with material supply.From the Loss in Weight per unit time of the bin, the actual flow rate is compared with the set point and the feeder is controlled in such a way that the actual flow rate corresponds accurately and consistently with the set point.During the refilling the feeder operates volumetrically by the control magnitude stored during the gravimetric period of operation.

Page 32: Polymer Plant Eqpt 1

Types of Loss-in-Weight Feeders

Vibro Feeder For Granular Material

Single Screws For Powdery Non-Sticky Material

Self Cleaning Double Screws For Powdery Sticky

MaterialSpirals or Double Spiral For Mixture of Pellets

& Powder

Page 33: Polymer Plant Eqpt 1

Why Loss in weight as compared to Volumetric Feeding?

Page 34: Polymer Plant Eqpt 1

SINGLE SCREW LOSS IN WEIGHT FEEDER

Page 35: Polymer Plant Eqpt 1

Types of Feeding Devices

Page 36: Polymer Plant Eqpt 1

Installation

Page 37: Polymer Plant Eqpt 1

Some more Installations

Page 38: Polymer Plant Eqpt 1

Belt Weigh Feeder

Page 39: Polymer Plant Eqpt 1

Working Principle of Belt Weigh Feeder

Belt load and belt speed signals are routed to the microprocessor-controlled measurement, control and regulation system, where they are processed and the actual feed rate is continuously compared with the set feed rate (set point) to assure that belt speed is controlled such that feed rate is maintained at a constant level.

Page 40: Polymer Plant Eqpt 1

Types of Feed Hoppers

Page 41: Polymer Plant Eqpt 1

Types of Feed Hoppers

Page 42: Polymer Plant Eqpt 1

Coriolis type Mass Flow MetersMeasuring principle

The Coriolis force is a force, which acts upon a moving mass on a rotation wheel. This physical law is the basis of Coriolis measuring systems. Feed material is fed to a measuring wheel running at a constant speed.

The Coriolis force acting upon the feed material is measuredwith high precision by integrated load cell and it is exactly proportional to the mass flow, even at varying bulk density and grain size.

Page 43: Polymer Plant Eqpt 1

Coriolis type Mass Flow Meters

P = feed rate [t/h]

MP =

• R 2

FZ = centrifugal force

FC

FR

FZ

M= torque = FC · R

= angular velocity [1/s]R = radius of measuring wheel [m]

FR = friction force

FC = CORIOLIS force

No impact to Fc

Page 44: Polymer Plant Eqpt 1

EXTRUDER & PELLETISERSystem Components:• Extruder (Barrel & Screw)• Diverter Valve• Gear Pump• Screen Changer• Die Plate• Underwater Pelletiser• Hydraulic Oil Unit• Hot Oil Unit / Barrel Cooling Water Unit• Lube Oil Units•Pellet Cutting Water (PCW) Unit

Page 45: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

• Largest Power Consumer In A Polymer Plant

• High Operating/design Pressure (~350 Kg/cm2g)

Page 46: Polymer Plant Eqpt 1

EXTRUDER & PELLETISERParameters For System Design

• Capacity (Kg/h)• Melt Flow Index (MFI) Range• Feed Inlet Temperature• Feed Volatile Content• Max Allowable Processing Temperature• Density• Product Pellet Size. Finishing requirements

Page 47: Polymer Plant Eqpt 1

TYPES OF EXTRUDERSBASED ON NUMBER OF SCREWS:Single Screw TypeTwin Screw Type

BASED ON DIRECTION OF ROTATIONCo-rotating TypeCounter Rotating Type

Page 48: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 49: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 50: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 51: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(MAIN DRIVE SYSTEM)

Main Drive

Process Side

Reduction Gear

Distribution Gear

Page 52: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(MAIN DRIVE SYSTEM)

Page 53: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(SPECIFIC ENERGY INPUT)

Specific Energy Input Vs Throughput

0.8 MFI20 MFI

Rate t / h

SEIkWh/kg

Page 54: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(BARREL HEATING / COOLING)

Steam ~ 40 bar

Water Water

Electrical Heaters

Page 55: Polymer Plant Eqpt 1

EXTRUDER & PELLETISEREXTRUDER & PELLETISER(BARREL HEATING / COOLING)(BARREL HEATING / COOLING)

Barrel cooling circuit for water cooling

Barrel heating circuit for steam heating

Page 56: Polymer Plant Eqpt 1

EXTRUDER & PELLETISEREXTRUDER & PELLETISER(BARREL HEATING / COOLING)(BARREL HEATING / COOLING)

Page 57: Polymer Plant Eqpt 1

Barrel Heating / Cooling Manifold

Page 58: Polymer Plant Eqpt 1

Barrel Heating / Cooling Manifold

Page 59: Polymer Plant Eqpt 1

Barrel Heating / Cooling Manifold

Page 60: Polymer Plant Eqpt 1

Barrel Junction Boxes

Page 61: Polymer Plant Eqpt 1

Barrel Junction Boxes

Junction boxes

Heater shells (wired up to junction boxes)

Cooling manifold (mounted)

Page 62: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 63: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(SCREW SHAFTS)

Page 64: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(SCREW SHAFTS)

Page 65: Polymer Plant Eqpt 1

2 Flight & 3 Flight Screws

3-flighted profile (Do/Di= 1.22) 2-flighted profile (Do/Di= 1.44 – 1.8)

Page 66: Polymer Plant Eqpt 1

SLOT CONTROL

Page 67: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 68: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 69: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 70: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 71: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER

Page 72: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(GEAR PUMP)

Page 73: Polymer Plant Eqpt 1

Gear Pump Cross section

Page 74: Polymer Plant Eqpt 1

Dual Pack Screen Changer

Filter Elements

Dual Cylindrical Slide Bars

Product Inlet

Hydraulic Actuators

Page 75: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(SCREEN CHANGER)

Page 76: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(SCREEN PACK)

Page 77: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(SCREEN CHANGER & DIE PLATE)

Page 78: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(DIE PLATE & CUTTER)

Page 79: Polymer Plant Eqpt 1

Typical Die Plate Cross Section

Page 80: Polymer Plant Eqpt 1

Multiple Row Design Twin Row Design Single Row Design

More Heat Transfer Area

Page 81: Polymer Plant Eqpt 1

EXTRUDER & PELLETISER(UNDERWATER PELLETISER)

Page 82: Polymer Plant Eqpt 1
Page 83: Polymer Plant Eqpt 1

PELLETISER CROSS SECTION

Page 84: Polymer Plant Eqpt 1

PELLETISER CUTTER SETTING

Page 85: Polymer Plant Eqpt 1

SPIN DRYER

Page 86: Polymer Plant Eqpt 1

SPIN DRYERProcess Water is removed prior to the Product reaching the rotating impact stage resulting in less power consumption. The two level design prevents the Rotor from agitating constantly in water, reducing component stress and eliminating the need for expensive and maintenance intensive shaft seals.

Once the majority of Process water is removed, the product enters the rotor where it is picked up and conveyed upward through the dryer

Air flow counter current to product flow is introduced in the upper portion of the dryer. This prevents the moisture from escaping with the product and further reduces the surface moisture level. Surface moisture removal can be achieved upto 500 ppm level.

Page 87: Polymer Plant Eqpt 1

SPIN DRYER

Page 88: Polymer Plant Eqpt 1

SPIN DRYER

Page 89: Polymer Plant Eqpt 1

BLENDERS

During production, variation in properties of product takes place due to various reasons. The customers demand a homogeneous product. Hence the need for Homogenising Blenders.

Types of Blenders:

Fluidised Silo Blenders (for Powders) Static Multi Tube Blenders (for Pellets)

Page 90: Polymer Plant Eqpt 1
Page 91: Polymer Plant Eqpt 1
Page 92: Polymer Plant Eqpt 1

BAGGING & PALLETISING Granular, Powder or Pellets Bagging &

Palletisation for Polymers

Types:Fully AutomaticSemi Automatic25 Kg. or 50 Kg. Bag1000 Kg. Big Bag ( FIBC)20000kg F IBC Bag inside containers

Page 93: Polymer Plant Eqpt 1

BAGGING & PALLETISING

Parameters For System DesignDesign Basis Production RateNo. of Days Per Year OperationNo. of Shifts Per Day Effective Hours Per ShiftWeight Of Each BagType Of SystemWeighing AccuracyFuture Expansion Provision

Page 94: Polymer Plant Eqpt 1

BAGGING & PALLETISING

System Specifications

Capacity , Bph / TphWeight of BagBag Specification / Type of Bag – Gussetted or

Pillow BagWeighing AccuracyMaterial CharacteristicsType Of Bag Closing - Sealing or StitchingPalletiser CapacityWrapping Requirement

Page 95: Polymer Plant Eqpt 1

BAGGING & PALLETISING

Machine System ComponentsWeighing Cum Tipping M/c (Net Weigher)Auto Bag PlacerStitching / Sealing M/cCheck Weigher / Metal DetectorInk Jet PrinterBelt ConveyorsPalletising M/cRoller ConveyorFork Lift TrucksShrink / Stretch Wrapping

Page 96: Polymer Plant Eqpt 1
Page 97: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING

Page 98: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING

Page 99: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(NET WEIGHER)(NET WEIGHER)

Page 100: Polymer Plant Eqpt 1
Page 101: Polymer Plant Eqpt 1
Page 102: Polymer Plant Eqpt 1

Type of Bag Closures

Page 103: Polymer Plant Eqpt 1

Bag Feed In Device

Page 104: Polymer Plant Eqpt 1

MOVIE CLIP

Page 105: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(STICHING MACHINE)(STICHING MACHINE)

Page 106: Polymer Plant Eqpt 1

Hand Stitching Machine

Page 107: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(CHECK WEIGHER)(CHECK WEIGHER)

Check weighers check packed goods as they run through for compliance with the stated weight. Incorrectly weighing packs trigger a signal for removal.

Page 108: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(METAL DETECTOR)(METAL DETECTOR)

Metal detectors are used for palletizing bags. They check the bags approaching the Palletizer for metallic foreign matter and if found positive, direct them to a bag removal station.

Page 109: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(BAG REJECTION / REMOVAL)(BAG REJECTION / REMOVAL)

Packages which are recognised as faulty are separated from the conveyed stream of packages via removal stations. They can be executed as swivel-mounted belt sidings, as a baffle or reject push-plate

Page 110: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(Bag Flattening)(Bag Flattening)

Sack flattening stations are positioned upstream of the Palletizers in order to produce the most evenly flat cuboid shape. They are composed of a belt conveyor as bottom belt and a height-adjustable, swivel-agitated pressure plate positioned above it, "irons" smooth the passing sacks. Depending on the bag fillings a model with vibratory bottom belt and a weighted pressure plate can be used.

Page 111: Polymer Plant Eqpt 1

Labelling and Coding UnitsLabelling and coding units apply details of

contents, loads or regulations on to packed goods or on to side surfaces of pallet-loads, mostly after stretching or shrinking. Computer controlled labelers print the labels and apply them as goods run past. Ink-jet coders inscribe the packages passing by with texts and markings using the ink-jet process. The imprints can be changed on-line by appropriately equipped devices, also automatically from package to package, e.g. for continuous numbering.

Page 112: Polymer Plant Eqpt 1

Labelling and Coding Units

Page 113: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(PALLETISER)(PALLETISER)

Page 114: Polymer Plant Eqpt 1

PALLETISERPALLETISER

Page 115: Polymer Plant Eqpt 1

PALLETISER

Page 116: Polymer Plant Eqpt 1

PALLETISER

Page 117: Polymer Plant Eqpt 1

PALLETISER

Page 118: Polymer Plant Eqpt 1

PALLETISER

Page 119: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(PALLETISER)(PALLETISER)

Page 120: Polymer Plant Eqpt 1

Airated Slide PlateAerated slide-plates and preceding intermediate balcony are used for palletizing of bags with a high sliding friction coefficient such as film sacks.

The air ( from regulated pressure fan) emanating from the perforated slide-plate surface forms a slide-air film which relieves the positioning and depositing of the bags.

Page 121: Polymer Plant Eqpt 1

Robotic Palletiser

Page 122: Polymer Plant Eqpt 1

Pallet Security through Stretching and Shrinking

Pallet loads are often exposed to considerable accelerative forces during transport and handling and must be protected from deformation, scuffing with adjacent loads and falling from the stacked load.

Stretching and shrinking of the pallets in plastic film are proven safety processes, with which the shipping goods are simultaneously protected against soiling and dampness

Page 123: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(SHRINK WRAPPING)(SHRINK WRAPPING)

The film cover, which becomes very stiff after shrinking, especially in the case of greater film-thicknesses, withstands considerable stress caused by accelerative forces.

Page 124: Polymer Plant Eqpt 1

Glueing UnitsGlueing units serve to stabilise pallet loads. By means of roll, brush or spray gun they apply a strip of glue on the packages as they run through. The anti-slip glue strengthens the palletized-goods layers , but permits depalletizing without damage to packages.

Page 125: Polymer Plant Eqpt 1

Palletless shipping units using the contour-hood shrink-wrapping system

The palletless shrink-wrap packaging replaces the pallet with the packaged goods themselves which becomes a self-supporting unit thanks to the shrink-wrapped cover. As a result not only is the significant expense for pallet use spared, but storage and transport space is also gained. Such packages are shipping units with integrated transport security.

They have great stability even under harsh transport conditions, can be easily handled with the usual harnessing equipment and protect their contents hermetically tight against moisture and dirt.

Page 126: Polymer Plant Eqpt 1

Slip Sheet Applicator

Papersheet applicator Film applicator

Film applicators are used either for feeding of stacking films as slip sheets or, in another version, for laying plastic films on empty pallets to protect the first stack layer from ground dirt and moisture. Another application is placing film or cardboard between the layers to stabilise the stack.

Page 127: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(FIBC BAG)(FIBC BAG)

FLEXIBLE INTERMEDIATE BULK CONTAINER

Page 128: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(FIBC LAYOUT)(FIBC LAYOUT)

Page 129: Polymer Plant Eqpt 1

Bag LoadersWhere bagged goods are to be loaded in the form of individual containers, bag loading machines may be used in order to attain economy and to control the physical demands put on personnel. Bag-loading can be almost completely automated with Autoloaders which stack the bagged goods directly onto truck loading surfaces or onto pallets placed on them.

Page 130: Polymer Plant Eqpt 1

BAGGING & PALLETISINGBAGGING & PALLETISING(AUTO LOADERS)(AUTO LOADERS)

Autoloader forms vehicle-wide layers of bags which are transferred by a stacking conveyor and forwarded to the loading head located over the vehicle loading surface. The loading head deposits the layers of bags on the vehicle and each time is lifted by one layer. After reaching the desired number of layers the Autoloader reverses by one stack length and positions the next stack.

Page 131: Polymer Plant Eqpt 1

Moveable Truck-loading Machines

Moveable truck-loading machines, for loading of vehicles with fixed body and of containers, can drive their long booms via the rear deep into the vehicle. The swivelling and inclineable telescopic loading belt at the boom end conveys the bags over the width of the vehicle to the depositing points.

Page 132: Polymer Plant Eqpt 1

Off-the-floor Truck-loading Machines

To load trucks in covered vehicle zones, moveable off-the-floor bag loading machines are installed on the building's roof located over the thoroughfare. The lowerable loading belt is moved down through a slit in the ceiling onto the open vehicle..

Covered vehicles are loaded with a machine onto which a linked conveyor is lowered through the ceiling slit, the conveyor loading the horizontally moveable loading belt in a height-adjustable belt-seat

Page 133: Polymer Plant Eqpt 1

Single and double jointed Wagon-loading Machines

For loading of covered railway wagons of the normal type, single jointed loading machines are used. Double jointed large volume loading-machines have a swivelling intermediate belt boom