GLASS REINFORCED PLASTIC PIPES
CONTINUOUS MANUFACTURING LINE
1 GENERAL ON CONTINUOUS GLASS REINFORCED POLYESTER PIPE PRODUCTION
2 G.R.P. PRODUCT CHARACTERISTICS
2.1 GRP Pipes Wall Description
2.2 End Couplings
2.4 Advantages in G.R.P. Application
2.5 Inspection and testing
3 RAW MATERIALS
3.2 Glass Reinforcements
3.3 Auxiliary Raw Materials
4 FACTORY DESCRIPTION
4.1 Production Capacity
4.2 Factory Layout And Installations
4.2.1 Total Extension
4.2.3 Sand Store and Feeding System
4.2.4 "E" And "C" Glass Fiber Distribution System
4.2.5 Resin feeding and mixing system
4.2.6 Utilities and Ancillary Installations
4.2.7 Electric Installations
4.2.8 Service Buildings
4.2.9 Open Spaces
5 PIPE MANUFACTURING PROCESS DESCRIPTION
5.1 Continuous Pipe Technological Process Description
5.2 Manufacturing production rate (mt/hr.)
6 PRODUCTION EQUIPMENT
6.1 Continuous F.W. Machine
6.1.2 Resin dosing station.
6.1.3 Polymerization Oven
6.1.4 Process Parameters Control Device
6.1.5 Computer Control of F.W. Machine
6.1.6 Gauging, chamfering and cutting device
6.1.7 Dust and Styrene suction system
6.1.8 Pipe lifting and supporting planes
6.1.9 Pipe antitorque supporting equipment
6.2 Sleeve Coupling Manufacturing Machine
6.3 GRP pipe sleeve joint joining equipment
7 PERSONNEL REQUIREMENT
7.2 Process Equipment Personnel
7.3 Fitting Manufacturing, Prefabrication, Testing and Handling
7.4 Total Manpower
8 TRAINING OF LOCAL PERSONNEL
8.1 Location Of Courses
8.2 Personnel To Be Trained And Course Duration
8.3 Preliminary Design
8.4 Know How And Engineering
8.4.1 Basic Design
9 TECHNICAL SERVICES AND PLANT COMMISSIONING
9.1 Plant Erection Supervision
9.2 Start Up, Commissioning and Training
9.3 Acceptance Test Procedure
9.3.2 Content and method
9.4 General Assistance
9.5 Running Assistance
9.6 Training on Site
10 EXCLUSIONS FROM THE SUPPLY
The present proposal covers the implementation of a new factory for the manufacture of glass reinforced plastic (G.R.P.) pipes through the establishment of :
- Continuous line for the continuous production of pipes with diameters from 300 to 2600
The project covers the
installation of the production facilities relevant to the manufacture of pipes
with diameters ranging from 300 up to
The G.R.P. pipe wall consists of three layers perfectly adherent with one another, each having different characteristics and properties in relation to their function. The properties of chemical resistance and impermeability are, anyway, equivalent for the three layers which are namely:
It is in direct contact with the conveyed fluid and guarantees the maximum resistance to the chemical attack from the fluid itself. Moreover, the liner presents an internal surface particularly smooth, without defects, cracks or delaminated zones. The liner is composed of one glass veil and one glass mat tape resin impregnated and is produced in two steps (inner liner and outer one)
§ filament or mechanical resistant layer:
Its function is to render the pipe wall resistant to the stresses due to the design conditions (stresses due to the internal and/or external pressure, flexural strength due to the external loads etc.) and generated by transport and laying operations. The thickness of the filament depend, then, upon the design conditions. The mechanical layer is composed of winded glass filament roving chopped glass, sand aggregate, glass mat reinforcement, all polyester resin impregnated.
§ gel coat or external layer:
It has a thickness of about
The pipe coupling is made by a GRP sleeve with continuous elastomeric gaskets with double or triple lips.
A wide range of fittings and special pieces can be manufactured in G.R.P. They present, therefore, the same characteristics, both chemical and mechanical, of the pipes. Fittings are manufactured manually employing male moulds or pipes pieces to be joined together. Ends of fittings can be bell and spigot type provided with sealing gaskets or plain type to be joined by welding to adjacent pipes or other fittings. The normal production of the new factory includes:
- 90° or 45° bends (by moulds)
- concentric and eccentric reducers (by moulds)
- fixed flanges and stub end (by moulds)
- blind flanges (by moulds)
Moreover, other special pieces such as manholes, flanged pipes equal and reduced tees etc. can be manufactured by welding together fittings and/or pipes sections.
Glass reinforced plastic pipes represent the ideal solution for the adduction of any kind of water, chemicals, effluent and sewers, because they combine the advantage of corrosion resistance, typical of plastics, with a mechanical strength which can be compared with the steel one. Typical properties that result in advantages in G.R.P. pipes application can be summarized as follows:
- Low weight of pipes lengths that allows for the use of light laying and transport means.
- Possibility of nesting of different diameters of pipe thus allowing additional saving in transport operations.
- Length of sections larger than other materials ones.
- Easy installation procedures due to the kind of mechanical bell and spigot joint.
- Corrosion resistance, both of the external wall in contact with the conveyed fluid. No protections such as coating, painting or cathodic are then necessary.
- Smoothness of the internal wall that minimizes the head losses and avoids the formation of deposits.
- High mechanical resistance due to the glass reinforcement.
- Absolute impermeability of pipes and joints both from external to internal and vice-versa.
- Very long life of the material virtually infinite, which does not need maintaining.
- Workability of the material in site employing simple equipment.
Before starting up production a check is made on the quality and characteristics of the resins relatively to the temperature and relative humidity in the production shops.
Optimum values of viscosity and temperature to be applied to the resin are pre-established, and the percentage of catalyst to be employed in the production phase is determined.
Controls in the production shops:
- control of lay-up (unit weight per square meter of resin and glass, type of resin and type of reinforcement)
- internal quality control
- check on the type of glass reinforcement used
- dimensional control of the positioning of the accessories according to technical specifications
- check on thickness
- Check on post-polymerization treatment (on continuous pipes). Continuous pipes manufactured are put into an oven having forced circulation of hot air and undergo heat treatment there. The purpose of this treatment is to complete the cross-linking of the resinous matrix. The degree of polymerization is directly related to the percentage of residual styrene monomer, which is established by laboratory analysis.
- Chemical tests: The quantity of styrol in the solution is deduced by comparing its peak with the peak of precisely known quantity toluene. A maximum of naught point two percent of free monomer is accepted (naught point five percent is permissible by law).
- Checking the weights: As it is withdrawn from the post-polymerization oven the product is weighed to ascertain the difference between the real weight and the weight foreseen in the theoretical construction sheets.
- Checking the Barcol hardness: Measurement of the hardness gives an indication of the degree of polymerization. This test is carried out on fifty percent of the products made.
The raw materials employed for the manufacturing of pipes are mainly polyester resins and glass reinforcements in the form of veils, chopped strands, woven roving and continuous filaments.
The polyester resins belong to the group of alkyd resins and present themselves in the form of colorless or slightly amber viscous liquids. In the commercially available state, the resin composition is represented by long linear chain, obtained by esterification of dicarboxyl acids with glycols and then dissolved in one or more saturated liquids monomers. One of the basic characteristics of polyester resin, is the presence of unsaturated bonds arising from the use of maleic anydride or other unsaturated components during the esterification. During pipes or tanks manufacturing, the resin hardens due to the polymerization reactions between the unsaturated radicals contained in the polyester chain. The resin then becomes a cross linked structure and assumes all the characteristics of thermosetting products such as, for example, the condensate of phenol, melamine or urea with formaldehyde. Polymerization reactions and hardening of resins, is promoted by special catalyst systems which are able to act even without the presence of high temperatures or pressure. The pipes and tanks production is in fact carried out at ambient temperature and atmospheric pressure. The mentioned cross linked bond can be represented by the following scheme:
A represents a polyoxydryl alcohol .
B represents an unsaturated acid
C represents an unsaturated product such as styrol
By varying the nature of the components of the resin (that is, by using glycols of different types and acids with a higher or lower weight) it is possible to obtain resins having different mechanical, thermal or chemical properties. The most employed resin in pipes manufacturing are the following:
· Polyester resins based on bisphenol or bisphenol A in a solution of styrol monomer.
Viscosity = 3.5 - 4 poises.
Reactivity = medium.
This type of resin provides good chemical inertness coupled to high mechanical strength in the laminate.
· Polyester resins based on isopthalic acid in a solution of styrol monomer.
Viscosity = 4 - 5 poises.
reactivity = medium to high.
This kind of resin assures good mechanical strength to the laminate and is the best solution, both under the point of view of economics, reliability and resistance for manufacturing goods to be used to transport any kind of water.
· Vinylester resins in a solution of styrol monomer.
This resin is employed when hot high corrosive products have to be handled and conveyed.
All the employed resins are, in any case, thermosetting type that means that the shape of the products, assumed after the polymerization, is not affected by heating and then high stability at temperature is assured. The same or different resins, if compatible, can be employed to manufacture the various layers of pipes.
Glass fibers are produced in the form of continuous filament, as per the following briefly described process. Various components are mixed together in order to obtain a basic compound characterized by a definite composition. The compound is then sent to a furnace, where is melted at high temperature so as to produce glass. The molten glass is then drawn into precision size controlled thin filaments. Filaments are successively processed into roving, mat, yarn or cut strands that are the basic reinforcements for the thermosetting resins. Glass necessary to produce pipes are the following:
· "C" glass tape.
It is in the form of veil with continuously and uniformly distributed fibers over the whole surface and with a porosity and stiffness such as to enable handling in the cutting and applying operations.
The veil is packed in rolls and presents
itself as a tape
The main characteristic of the veil is the high chemical resistance and is, in fact, employed to manufacture the first layer of the liner of pipes (inner liner).
· "E" glass chopped strand mat tapes.
It consists of chopped glass fibers not woven. The chopped fibers are distributed without any preferential orientation but in order to assure a regular specific weight to the tape.
The fibers are bonded together with a
polyester base binder. The mat tapes packed in rolls, present a width of
· "E" glass filament roving.
It consists of strand of continuous glass
filament roving supplied in rolls. More parallel strands are employed to
manufacture the mechanical resistant layer of pipes. Density or size of roving
is defined in grams per kilometer of single filament (
Filaments are sized with a special sylan finish that imparts a taping effect to improve the efficiency in winding operations.
· "E" glass woven roving tapes.
It is a tissue made of strands of continuous filament roving oriented in the two main directions.
They are treated with binders in order to impart excellent adaptability to the shape of the moulds without any wrinkling, empty spaces or irregular dripping of the resin to be applied.
The woven roving tapes are employed to manufacture the mechanical resistant layers of hand made fittings.
The auxiliary raw materials are necessary, in limited quantities, to promote or inhibit the polymerization reactions in order to better control and select the working phases both for pipes. Ultraviolet rays inhibitor agents are employed to increase the already great resistance to weathering.
The main auxiliary raw materials are namely:
· Catalyst for polyester resins: 50% solution of methyl ethyl ketone peroxide in dimethylphtalate.
· Accelerator : solution of cobalt naphtenate in styrene.
· Inhibitor : 10% solution of ter-butyl-catechol in styrene.
· Thixotropic agent : micronized silica gel.
· Solution of paraffin in styrene.
· Polyvinyl alcohol.
· U. V. rays inhibitor.
· Silica sand
Range of producible pipes and factory capacity, are sized in order to satisfy the local needs of potable water lines and networks, irrigation and sewer systems.
The proposed factory
is sized for an average manufacturing capacity of 12000 ton/year of finished fiberglass
pipes with average diameters of 300 -
2600 mm, dia.
The factory should cover a rectangular
shape plane area of about
The manufacturing unit consists of steel or reinforced concrete structure shed of rectangular shape plan and is divided into a process area and service zones.
The shed of the process area is sustained
by two rows of columns providing
The floor is made of leveled concrete
The shed covers the following installations:
- Process area for pipes:
Process area for pipes including bell coupling
One overhead traveling crane (5 tons capacity)
Fittings manufacturing area
- Services areas:
Resin mixing room
Glass storage area
Warehouse (shelves, welding and drilling machine, grinders and tools, spare parts).
Quality control laboratory
Dressing rooms, showers and toilets
Pressure test equipment for pipes
Sand storage silos should have at least 150 ton capacity. The sand is transferred to the filament winding machine sand distributor by means of a screw feeder.
The fiberglass coils are assembled on steel frames and the fiber threads are fed to the filament winding machine through ring guides and tensioning device.
Resins are stored in suitable underground tanks (120 ton capacity at least) and are conveyed to the daily feeding tank by means of polyethylene pipes.
There, resins are added with Cobalt Naphtenate and mixed by means of electric blade stirrers, driven by the control panel of the continuous F.W. machine, with continuous electronic control of the operation in respect of temperature and flow of various components.
By means of suitable dosing pumps, resin are then pumped and conveyed to mixers where they are further added with organic peroxide and then, by free-fall, used in the production process.
The manufacturing shed should be completed with the following utilities and ancillary installations:
· Fire fighting network, hydrants and hose reel boxes.
· Wall mounted powder or CO2 extinguishers.
· Fire fighting diesel pump (one unit).
· Fire fighting electric jockey pump (one unit).
· Concrete raw water reservoir.
· Potable water network.
· Raw water pump (one unit).
· Raw water network.
· Sewer network.
· Shed venting systems.
· Glass powder suction system.
· Hydraulic test equipment facilities.
· Two frontal fork lift 3 ton capacity and one side fork lift 10 ton.
· Fence and gates.
The positioning of the utilities equipment is shown on drawing attached herein. Brief description of some utilities is given here below:
· concrete reservoir:
The concrete reservoir contains the water necessary for the fire fighting system and raw water consumption. Water to the reservoir is fed by means of a 2" pipe sectioned, at factory battery limits, by locked open gate valve installed in pit.
The capacity of the reservoir is about
· fire fighting system:
The fire fighting station is composed of one diesel engine operated pump and an electric motor jockey one. The diesel engine is provided with its own fuel daily tanks.
Foreseen head and flow rate of the diesel
engine pump are respectively
When pressure in the fire fighting network reduces below 3 bar, the diesel pump automatically starts and will be stopped by manual operations. Hydrants are distributed along the 8" fire fighting ring, each provided with two hose connections.
The hoses are contained in boxes located nearby the hydrants.
· compressed air system:
Envisaged flow rate is 5,000 l/min. at 7 bar. Compressed air piping, inside the shed, is composed of 2" pipes rings running on steel structures and provided with 1" shed crossing pipes, installed inside the ducts and wall mounted connections.
· potable water:
The potable water is fed by a 2" pipe, sectioned at factory battery limit by a gate valve installed in pit and is directly conveyed in the factory network.
Potable water feeds the office building area, the toilets of the shed and the test and laboratory rooms.
The total electrical power installed is 400 KVA and considering a contemporaneity of 75% the required power is 300 KVA about.
The main electric installations inside the fence of the factory are then the following:
- General electric switch board and control panels.
- Power sockets (
- lighting system inside and outside the shed.
- earthing system.
The diesel generator is located under an own steel shelter and is completed with its own daily tank. Lighting inside the shell is realized by means of roof mounted mercury vapors lamps, 250 W each. Every six meters of shed, two lamps are foreseen.
The following buildings are envisaged to be installed inside the factory area:
- One prefabricated or masonry building suitable for the accommodation of 10 employees and one manager. The building is provided with office furniture and toilet.
- One prefabricated building for resin
drums depository (20 x
- Two block houses (2,5 x
Moreover, a cover for vehicles is foreseen
Not covered spaces extend for about
The factory area is fenced and provided with one main and two services gates.
The manufacturing process is based on the filament winding technique and complies with A.S.T.M. code D 2996 (Standard Specification for Filament Wound Reinforced Thermosetting Resin Pipes) type 1, grade 2, class E and ASTM D3517, ASTM D3754, ASTM 3262, BS 5480:1990, AWWA C950, AWWA Manual M45
The manufacturing process proceeds step by step as follows:
The continuous production of GRP pipes through the filament winding process, avails itself of a mandrel which surface is made of a steel tape moving longitudinally with a speed depending on the tape width.
The band is elycoidally wound on suitable supporting bearing placed along the mandrel.
A defined number of pushers, driven by a suitably shaped cam plate, moves the steel band longitudinally.
A special mylar release film, protecting the surface of the mould and useful during extraction operations, is applied to the mandrel. Then, a ply of chemical resistant "C" glass is laid up the mandrel. This glass reinforcement, suitably impregnated with liquid resin, will be the chemical-resistant inner liner of the pipe, being rich in resin (90% resin, 10% glass) and having a predetermined thickness.
The final layer (external liner) will have the same characteristics as first.
Two other layers are applied between the first and the last ones:
a - an anti-diffusion barrier made of 70% of resin and 30% of chopped glass (second liner)
b - a mechanical resistant layer which thickness, composition and glass yarns disposal depend on the mechanical characteristics required for the pipe
These internal layers consist of the following raw materials:
- Chopped glass yarns
- Continuous glass yarns (roving)
- Silica inserts, if needed.
The continuous roving, circumferentially
wound, assures the required circumferential resistance, while the function of
the chopped glass (chopped glass yarns 25-
The silica inert, when applied, increases the stiffness characteristics and the pipe wall thickness, without exceeding the quantity of glass foreseen.
The chopped roving is laid on the pipe surface through the slit of a hopper placed upon the mandrel. The glass yarns conveyed from the feeding units are then chopped using a suitable cutter. The required quantity of chopped glass applied to the pipe wall will be achieved by combining the cutter rotating speed (quantity of chopped glass produced) with the mandrel surface translating speed (being finally the rotating speed of the mandrel).
The continuous glass yarns, supplied by the feeding units, are hoop-wound on the manufacturing pipe by driving the roving through some tensioning devices, thread guides and distributing rack. The required quantity of continuous roving can be obtained by defining the suitable number and substance of yarns, while disposal of yarns in the different pipe section layers can be suitably arranged by modifying the position of the yarns in the thread guides and in the distribution rack.
The silica inert, if required, is applied through the slit of a hopper placed upon the mandrel and is batted by modifying the rotating speed of a knurled cylinder placed peripherally to the hopper.
The resin is supplied and applied to the mandrel surface by means of two special feeders equipped with suitable gauged holes. One of the feeders supplies the resin required for the manufacturing of the chemical resistant inner liner and anti-diffusion barrier. The other has the function of supplying the resin for the mechanical resistant layer and external liner. The adoption of two feeders for the manufacturing of the different layers allows using two resins for the same pipe bar.
The feeders contain resin which is already mixed with catalyst in the due proportion. Mixing operations are carried out in two different mixers, one for each feeder. Resin and catalyst are delivered separately to the mixers by means of batching pumps. The quantity of resin and catalyst required, as for other raw materials, depends on the mandrel speed and is defined through a suitable electronic batching system.
Polymerization of the resin (hardening of the product) is carried out in an oven with 4 differentiated areas with radiant heating units. For each area the heat to be supplied can be controlled so that the assure the maintaining of the required values of jellification, isothermal peak and post-polymerization in the oven.
The production line is equipped with gauging and automatic cutting device.
The pipe cutting at the required length is made by means of a diamond disc tool following the progress of the product.
After cutting, the pipe bar is automatically moved away through three lifting tables
Whenever required, pipes manufactured are subjected to an hydraulic pressure test: each pipe bar is filled with water and then, by means of a suitable press, its internal pressure is increased up to 1.5 or 2 times more than the nominal pressure the pipe should withstand. The press structure is able to withstand a max. axial thrust of 1000 ton.
Moreover, all pipes produced are subjected to a careful quality control by means of systematic non-destructive tests as:
- Thickness measurement
- Barcol hardness measurement
- Visual examination
In addition to the above, some samples are subjected to the following destructive tests:
- Parallel plate press test
- burst test
- Fire resistance test
- Axial tensile stress test
- Axial and circumferential bending test.
Both destructive and non destructive tests are carried out according to ASTM (American Society for Testing and Materials) standards.
The quality control on the final product is preceded by a careful production process and raw materials control. For example, with respect to resin, controls are made on viscosity, reactivity, styrene content, elongation to rupture. With respect to silica inerts, granulometry, humidity content, silica and iron content are checked. For glass, controls are made on external aspect, humidity content, losses after calcining, roving stiffness, resistance to grinding.
Production on 3 shifts x 220 working days
The manufacturing of continuous pipe is carried out by a continuous mandrel. This is formed by winding a continuous steel tape over an horizontal beam. The steel tape translates in the axial direction while the mandrel is rotating. The steel tape returns at the end of the beam and is driven into the mandrel inner empty section. It is then wound onto the opposite end of mandrel again. In this way the steel tape forms a smooth surface mandrel rotating with simultaneous advancing in the axial direction.
The laminate is applied onto the moving mandrel.
First a release film, e.g. polyester film, is wound on the mandrel, followed by a surfacing mat. Filament winding, together with chopped glass, sand aggregate and polyester resin are applied simultaneously. Finally a new layer of surfacing mat is applied.
According to the process philosophy, the layer applied next to the steel tape represents the chemical resistant inner layer, while the material supplied next to the curing ovens is the mechanical resistant outer layer. The laminate building-up can thus easily be made in compliance with the appropriate design by controlling the amount and position of various materials applied.
After the curing oven, the pipe is automatically cut to required length by a suitable sawing unit.
No moulds are required in the continuous pipe production process but only a mandrel which diameter can be modified according to requirements.
The main components of mandrel are:
- Steel tape
- Aluminum stripes
- Disc plate support
- Steel tape return device
- Main shaft (two sizes are supplied to cover ND 300-600 and 700-2600)
- Steel tape tensioning device
The resin is supplied and applied to the mandrel surface by means of two special feeders equipped with suitable gauged holes. One feeder is foreseen for liner layer and other for mechanical structure layer. Such feeders contain resin which is already mixed with catalyst in the due proportion. Mixing operations are carried out in two different mixers, one for each feeder. Resin and catalyst are delivered separately to the mixers by means of double head dosing pumps. One pump is foreseen for liner resin and catalyst delivery , the other is foreseen for mechanical structure resin and catalyst delivery . The quantity of resin and catalyst required, depends on the mandrel speed and technological process .
The system includes:
The polymerization oven is placed on line with the advancing mandrel.
There are 9 longitudinal heating and reflecting sections placed over 18000 angle arc.
Each segment can be shifted ..
The oven is equipped with suction hood for styrene emission and heat over flow system.
The control and supervision of production cycle is made by computer connected to a PLC device controlling physical variable as material parameters (flow, temperature, tensioning etc.) and heat flow of oven and connected to a CNC device controlling the operation of filament winding machine.
It is possible to control the production process through the following parameters:
Gauging, chamfering and cutting operations are automatically made without any personnel requirement, by means of a tool holding trolley, placed out of polymerization oven, having the same longitudinal advancement speed of the pipe.
Such trolley is able to
Powders coming from gauging, chamfering and cutting operations are automatically sucked and conveyed to a particular device providing, ..
After curing and when exiting from the polymerization oven, the pipe is supported by three planes equipped with free-wheels ensuring rotation and advancement of the pipe itself.
The second plane is equipped with a special device rotating the pipe during cutting operation.
After cutting, the three planes simultaneously translate along pipe direction, .
This equipment is of great importance for the production of heavy weight FRP pipes (large diameters and high stiffness).
The system consists of a double twin wheels acting as additional supporters of the pipe during its rotation and yelding a positive torque balancing the negative momentum caused by the pipe rolling friction.
The following materials are supplied:
- Rubber coated wheel ..
The sleeve couplings are made by resin impregnated E glass roving wound on a steel wheel mandrel over which a elastomeric gasket with double or triple lips has been placed.
These wheel mandrels are made of two half pairs: one half is assembled on a axle rotating by mean of motovariator and the other half assembled on a piston axle of a pneumatic cylinder.
As soon as the axle of the piston is backward it moves back half with mandrel and therefore the bell coupling can be extracted.
The bell coupling machine has two manufacturing positions to be operated at the same time and it is assembled as follows:
· two rotation axles assembled ..
This machine allows the operators to join the FRP plain end section to the sleeve joint bell coupling.
The machine is equipped by one shifting end
plate in order to operate for different FRP pipe section length and pipe
diameter; it can be applied for length ranging from 2 mt up to 16 mt and for
diameter ranging from
The equipment consists of the following main mechanical parts:
Here below is reported a short description of the machine:
After the system has been settled according to the requested pipe length by shifting horizontally the shifting end table, the pipe is supported by the two lifting tables and positioned by adjusting vertically the pipe so as to move the centerline pipe to the end plates and sleeve joint center point.
When the GRP pipe and the sleeve joint are definitely positioned, the fixed end plate operates hydraulically in such a way to develop the thrust requested by the sleeve joint bell coupling friction during the joining stage.
Mechanical maintenance needed by the plant shall depend on the effective working hours and on the pipe diameters produced. Maintenance usually consists of:
Staff and workers requirement for the G.R.P. pipes factory is set here below.
Plant Management And General Services Personnel
- Guard and drivers
- Technical service
(required number for three shifts)
- F.W. operator
- bell operator
- Electricians and mechanics
Continuous line (required number for three shifts)
- Foreman and leading operator
- Laboratory operator quality control
The personnel of the factory is then composed as follows:
- manager 1
- superintendent 3
- clerks/ workers 30
Course of training in management, operation and maintenance of the new factory, will be ..
Training courses will be held at Buyers factory directly on equipment, ,
On the basis of the personnel requirements for the factory correct operation and managing, it is considered .
KNOW HOW, ENGINEERING DESIGN AND DOCUMENTATION SUPPLIED
It includes a preliminary layout of plant based on its working flow-sheets, as well as the complete list of machines and tools needed for production and relevant to both process and facilities.
This preliminary design will be consolidated into a Technical Report, which will include also all data relevant to production yields, as well as a detailed costs estimate.
Based on the above document, the supply of the know-how and engineering shall consist of the following documents referred to the plant as described in the Technical Report.
· Design Of Civil Works
· Mechanical Design
· Electrical Design
· Executive And Detailed Design Work
· Machines To Be Supplied Technical Description
· Operating Handbook
· Engineering Handbook
All the above documents, except the ones for mass-produced equipment, will be supplied in English language.
We will supervise the works relevant to the erection of the plant.
Start up and commissioning of the whole plant will be provided by a team of experts as follows:
- 1 plant superintendent.
- 1 continuous filament winding machine specialist.
The above team will also undertake training of operating personnel at site in order to enable them to operate the machine independently and in optimum way .
The purpose of the acceptance tests is to prove completeness,.
The technicians of both parties shall carry out in customer's country
Definition of idle test run:
At first, each machine and equipment supplied by us shall be tested.
Definition of production run:
During the production run one (1) piece of typical products, shall be manufactured by.
Both parties shall complete the tests within.
We will supply you with all standards, specifications and shop drawings relevant to pipes of each class, diameter and service pressure series.
Moreover our design office will be.
We shall place at your disposal, for the length of time specified above, our experienced personnel as needed for the running operations of the plant. Furthermore we will supply.
We will assist the customer in training the latter's specialists, in customer's plant, for a period.
Purchase of industrial area, urbanized and leveled, with connection to power, telephone and water system, construction of industrial buildings and offices are not included in the supply.
Moreover, the following general services and utilities should be provided on site and should be at Customer's charge:
PROGRAM BAR CHART
0 APPROVAL OF THE CONTRACT
OF PROCESS MACHINERY IN
2 DESIGN OF THE PLANT
3 CONSTRUCTION OF BUILDING AND UTILITY PLANT IN LICENSEES COUNTRY
4 TRANSPORTATION OF PROCESS MACHINERY AND LOCALLY MANUFACTURED EQUIPMENT TO THE INSTALLATION SITE
6 TESTING AND START-UP