ergil catalogue

Page-1

Storageteck is registered trademark of Ergil Group

Head Office:M.Nezihi Ozmen Mah.Fatih Cad.Kayikci Sk.No.8 K:2 Merter-ISTANBUL /TURKEY

Phone: +90 212 643 62 26 (Pbx) Fax: +90 212 643 62 22 Dubai Office:Rak Free Trade Zone P.O.Box:10559 Ras Al Khamiah U.A.E

Factory:Atatürk Cad.OSB.Fatih Sitesi 6/a Blok Ikitelli-ISTANBUL/TURKEY www.ergilgroup.com [email protected]

FORWARD

About Ergil Group

Ergil Group International, is one of the Middle East's largest providers of products and services to the oil and gas industries. Since 1982, The Company adds value through the entire lifecycle of oil and gas reservoirs and provides and integrates products and services. ERGIL GROUP COMPANIES, construct all kind of oil or liquid storage tanks and manufacture their accessories. Company has already involved this kind several oil storage tank projects in Turkey and Middle East before. Ergil Group Companies includes, but not limited to storage tank equipment, such as flame arresters, breather valves, gauge hatches, floating roofs, and absorption branches, but also provides many other products for energy industry, pig receiver and launchers, heat exchangers, silencers, fire extinguishing systems, cathodic protection service and products are only some of them. With customers like BP, Shell, Total, Energy Petrol, Opet, Petrol Ofisi and Tekfen Ergil is a brand name in the storage and transportation of petroleum and liquid chemicals, production of storage tank equipment, and corrosion control systems. ERGIL GROUP Companies has developed an excellent reputation internationally in the industry because of our total commitment to quality in every aspect of the business. Beginning with raw materials through process production and delivery, ERGIL GROUP has always insisted on the highest possible quality associated with the product lines. Today, our well educated and experienced employees service the needs of Ergil's global customer base markets. In addition to its headquarters in Istanbul, TURKEY, Ergil has branch office in capital of Turkey, Ankara, and direct sales office in many countries such as USA, Germany, Pakistan, Iran, Syria, and Malaysia. Ergil is certified two EN ISO 9001 : 2000, a model for quality assurance for companies involved in the design, development, manufacturing, installation, and servicing of products.

Atatürk Caddesi Organize Sanayii bölgesi. Fatih Sitesi 6/A 34670 Blok –İkitelli –İstanbul_TURKEY

Tel: +90212 485 40 07 Fax: +90 212 485 40 42- Web: www.ergilgroup.com

e-mail:[email protected]

Page 2 of 146

EN ISO 9001:2000

INDEX

OUR ORGANIZATION CHART 1

OUR ACTIVITY FIELDS 2

OUR CERTIFICATES 3

ABOUT THE CORROSION AND CATHODIC PROTECTION 4

OUR ACTIVITY FIELDS OF CATHODIC PROTECTION 5

OUR CATHODIC PROTECTION REFERENCES 6

OUR FLOATING SUCTION PIPE REFERENCES 7

OUR INTERNAL FLOATING ROOF REFERENCES 8

OUR TANK AND PIPING REFERENCES 9

PRESSURE VESSELS 10

PıG RECEIVER / LAUNCHER AND REFERENCES 11

TANK ACCESSORIES 12

OUR VEHICLES 13

FIRE FIGHTING EQUIPMENT 14

OUR FIRM REFERENCES 15

PRODUCT DETAILS 16

WE REPRESENT 17

REPRESENTATIVES 18

BROCHURE 19




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EN ISO 9001:2000

SECTION -1 4 SECTION -2 6 SECTION -3 9 SECTION -4 14 SECTION -5 36 SECTION -6 41 SECTION -7 45 SECTION -8 48 SECTION -9 52 SECTION -10 85 SECTION -11 93 SECTION -12 96 SECTION -13 121 SECTION -14 132 SECTION -15 138 SECTION -16 140 SECTION -17 141 SECTION -18 144




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EN ISO 9001:2000

SECTION -1

OOOUUURRR OOORRRGGGAAANNNIIIZZZAAATTTIIIOOONNN CCCHHHAAARRRTTT

ERGİL GROUP ORGANIZATION SCHEME

General Manager

Assistant of General Manager

Quality Agent of Management

Administrative &Financial Trades

Manager

Sale & CostumerRelation Manager

Project GroupManager

Design & ProjectManager

ProductionManager

Quality AssuranceManager

Responsible ofAccountancy &

Personnel

Responsible ofNatural Gas

Project &Application

Technical DrawingConstruction

Production Chief Responsible ofInput Control

Responsible ofBuying

Responsible ofCathodic

Protection &Application

Responsible ofMetalfilingProduction

Responsible ofProcess Control

Responsible ofWelding

Construction &Application

Responsible ofAssembly

Responsible ofDocument

Responsible ofStore

Responsible ofUrgent State

Responsible ofPeriodic Cares

Responsible ofAfter Sale Duty

General Coordinator

Responsible ofOffer Cause

APPROVED: KERİM ALTUNERGİL REVISION NUMBER: 3 REVISION DATE: 05.08.2003




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EN ISO 9001:2000

SECTION -2

OOOUUURRR AAACCCTTTIIIVVVIIITTTYYY FFFIIIEEELLLDDDSSS




Page 7 of 146

EN ISO 9001:2000

MANUFACTURE OF FUEL TANK ACCESSORIES

Pressure Vacuum Vent (TSEK-06/3014 ) Flame Arrester ( TSE 35-6-EX.K./024 ) Gauge Hatch

o Unlocking type o Locking Type o Non-atmospheric Gauge Hatch

Floating Suction Pipe Pig Receiver Pig Launcher Pig signaller By Pass Valve (Including top of the Fuel Pump) Blende Type Interrupter Fuel Filtering Vessels Pipeline Flow Indicator Check Valves Tank Level Indicator Quick Closer for Pig Receiver and Launcher

MANUFACTURE OF FIRE PROTECTION ACCESSORIES

Foam Expulsing Systems. Foam Expulsing Ball Fire Foam Nozzles, Fire Fuse Foam Skimmers, Mixing Apparatus

NATURAL GAS

Measurement Station for Pressure Reduction and Restriction (SKIT)-( SEK-35-14.02/851 )

Isolated Coupling Manufacture of Diesel Fuel Injector Testing Devices (BOSCH Type)

CATHODIC PROTECTION CONSUMABLES

SPECIAL MANUFACTURES Silencer Went Stack ınline Flame Arrester End of Line Flame Arrester




Page 8 of 146

EN ISO 9001:2000

UNDERTAKING GROUP – ACTIVITY FIELD

MANUFACTURE OF FUEL TANKS – According to API 650 MANUFACTURE AND MAOUNTING OF INTERNAL FLOATING CEILING

CATHODIC PROTECTION

Study, Projecting Cathodic Protection for Fuel Pipes Cathodic Protection for Inner and Outer Bottom of Tanks Cathodic Protection for Quay Legs and Floats Cathodic Protection for Boiler and Heat Exchanger Manufacture of Joint Set and Insulated Flange,

NATURAL GAS

Etude, Design, Projecting Intercity Steel and PE Distributing Lines - Within the scope of

Infrastructure Adequacy of ıGDAŞ, EGO Steel Pressure Lines – Within the scope of Infrastructure Adequacy

of BOTAŞ A and B Type Stations for Pressure Reduction Transformation of Industrial Plants Agency and Dealership for Manufacturing Companies in and out of

country




Page 9 of 146

EN ISO 9001:2000

SECTION -3

OOOUUURRR CCCEEERRRTTTIIIFFFIIICCCAAATTTEEESSS




Page 10 of 146

EN ISO 9001:2000




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EN ISO 9001:2000

IEP ULUSLARARASI ENER.Ii Pc0znriM srRTirixasYoN vE TEKNI

onclwizASYoNU

Il.

RefNo;EP.08.03.07 i ] . , iSubject: ATEX Application About I

-' 'l

lERGiL GRUP lml. ith. ihr. san' Tic. Ltd. $ti. lrSTAI{BUL/TURKEY ]

About: Your ietter with REF:ERG.Y.I14.07 Date: 07,03.2007 ]l

' On your relevant letter you are asking for information aboutlyour appliance for below products to

[urdp& Union ipproved organization FtZU wich we are an reRresantative according to the ATEX 94/9.

Your application for Flame A:resters and Pressure Vacuum lVents is on evaluation stage.I

Testings and experiments according to the harmonized stanparts wich are bbunded up in ATEX

insnuctions are finiihed.Your certification procedure will be completed {fter some morelexperiments.

Your appliance for cerlificate to FTaIJ and its scope is defi{red below;

i-End of Line Arrester EEFA-PW Series2-Gauee Hatch Gh,GH'L Series

Web




Page 14 of 146

EN ISO 9001:2000

SECTION -4

AAABBBOOOUUUTTT TTTHHHEEE CCCOOORRRRRROOOSSSIIIOOONNN AAANNNDDD CCCAAATTTHHHOOODDDIIICCC PPPRRROOOTTTEEECCCTTTIIIOOONNN




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EN ISO 9001:2000

PREFACE

The raising use of metals, being accompanied with industrial development in

our country, brings about economic loss as well as extravagance of resources

and of materials, which cannot be recycled due to lack of prevention of

corrosion. The rate of corrosion loss, being one of the most important causes

of extravagance, increases sharply. In our country, surrounded by sea from

three directions, mostly marine metal structures are not protected sufficiently.

Since necessary precautions are not taken, every year huge corrosion losses

take place.

The large parts of pipelines, that contain such liquids as petroleum, water,

natural gas either are protected or controlled insufficiently. Besides due to

lack of coordination with different constituents, separated activities cause

underground network to be all mixed up like spider’s web. The presence of

protected and unprotected systems in the same area result in a complex form

so new systems serve as an anode of former systems.

One of the must significant reasons why our company is established is to

initiate the inevitable activities that enable to prevent corrosion failure

effectively and thus contribute to country’s economics. Doing scientific

research, benefiting from universities to determine the most appropriate and

affective means of protection system to prevent metallic corrosion, and to

acquaint scientific knowledge to domestic industries is the main goal of our

company.

It is believed that introducing our catalogue prepared for above mentioned

goals will assist in preventing corrosion.

Regards,




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EN ISO 9001:2000

FUNDAMENTALS AND PREVENTION OF METALLIC CORROSION

Corrosion is defined as a gradual wearing away or alteration by chemical or

electrochemical oxidizing process. Since the process of corrosion returns metal to its

original conditions, we must consider the action degeneration in its true primary

form.

Ordinarily, iron and steel corrode in the presence of both oxygen and water. Rapid

corrosion may take place in water; the rate of corrosion is accelerated by the velocity

or the acidity of the water, by the motion of the metal, by an increase in temperature

of aeration, by the presence of certain bacteria, and by other less prevalent factors.

On the other hand, corrosion is generally retarded by protective layers (or films)

consisting of corrosion products or absorbed oxygen; high alkalinity of the water also

retards the rate of corrosion on steel surfaces.

For instance, corrosion of steel does not occur in dry air as is negligible when the

relative humidity of the air is below %30 at normal or lower temperature. Prevention

of corrosion by dehumidification is based on this fact.

All structural metal corrode to some extent in natural environments. Bronze, brasses,

stainless steels, zinc, and aluminum corrode so slowly under the service condition in

which they are placed that they are expected to survive for long periods without

protection. Corrosion of structural grades of iron and steel, however, proceeds

rapidly unless the metal is amply protected. This susceptibility to corrosion of iron

and steel is of great concern because, owing to favorable cost and physical prepay

considerations, vast quantities are used. Annual losses due to corrosion of steel

have been variously estimated at

Nearly $70 billion in the United States. It is apparent that protection against

corrosion of iron and steel is an indispensable phase of sound engineering.




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EN ISO 9001:2000

MECHANISM OF CORROSION Corrosion in metals, whether in the atmosphere, underwater, or underground, is caused by a flow of electricity from one metal to another metal or recipient of some kind; or from one part of the surface of one piece of metal to another part of the same metal where conditions permit the flow of electricity. Types of corrosion commonly identified on metal Uniform Electrochemical Galvanic Concentration cell Corrosion fatigue Intergranuler Erosion corrosion Stress corrosion ELECTROCHEMICAL CORROSION The cell in Figure 1. Illustrates that corrosion process in its simplest form. This cell includes the following essential components. A metal anode A metal cathode A metallic conductor between the anode and cathode An electrolyte (water containing conductive salts) in contact with anode and cathode but not necessarily of same composition at the two location

Metalic cunductor wire

Anode

Oxidation reactionoccurs at anode

Current flow in conductor

Cathode

Electrolyte(conductive solutions)Reduction reaction occursat cathode

Current flow through the electrolyte

Figure .1: Simple cell showing components necessary for corrosion If the cells as shown were constructed and allowed to function, an electrical current

would flow through the metallic conductor and the electrolyte. The anode would

corrode (rust, if the anode were iron); chemically, this is an oxidation reaction.




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EN ISO 9001:2000

Simultaneously, a nondestructive chemical reaction (reduction) would proceed at the

cathode, producing hydrogen gas on the cathode in most cases

However, oxygen or some other depolarizing agent is usually present to react with

the hydrogen, reducing this effect, so the cell would continue to function. If the

metallic conductor were replaced with a voltmeter, a difference of potential could be

measured between the electrodes.

The difference in potential that causes this electric current is due mainly to contact

between dissimilar metallic conductors or differences in concentration of the

solution, mainly with respect to dissolved oxygen in natural waters. Almost any lack

of homogeneity on the metal surface or the in its environment may initiate attack by

causing differential in potentials that results in more or less localization of corrosion.

Many other facts are involved, but these include most of the important fact known

about ordinary corrosion and are all satisfactorily explained by application of

electrochemical principles, the metal undergoing electrochemical corrosion need not

be immersed in a solution, but may be in contact with moist soil, or patches of the

metal surface may be moist.

Technical definition of electrolyte

An electrolyte is a solution containing ions, which are particles bearing an electric

charge. Ions are present in solutions of acids, alkalis, and salts.

It is well known that the formation of rust by electrochemical reactions may be

expressed as follows:

1. 4Fe Ý 4Fe2+ + 8e-

4Fe + 3O2+2H2O Ý2Fe2O3.H2O (hydrated red iron rust)

2. 4Fe + 2O2+4H2O Ý4Fe(OH)2 (red iron rust with water).

4Fe(OH)2+O2 Ý2Fe2O3.H2O +4H2O (hydrated red iron rust)

According to a number of investigations, the most stable form of rust is Fe2O3. At

higher temperatures (900 to 1300oF) Fe2O3, revert, Fe3O4




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EN ISO 9001:2000

GALVANIC CORROSION

Better known as simply dissimilar metal corrosion, this form of degeneration pops up

in the most unusual paces and often causes the most painful professional

headaches.

The Galvanic Series of Metals guide details how the galvanic current will flow

between two metals and which will corrode when they are in contact or near each

other in the ground.

The driving force (difference of potential) available to promote the electrochemical

corrosion reaction of reflected by the galvanic series. This is a list of a number of

common metals and alloys arranged according to their tendency to corrode

galvanically. Metals grouped together do not have a strong effect on each other, and

the farther apart any two metals appear, the stronger the corroding effect on the one

higher in the list. It is possible for certain metals to reverse their positions in some

environment, but the list as given will hold generally in natural waters and

atmosphere (The galvanic series should not be confused will the similar

electromotive force series, which shows exact potentials based on highly

standardized conditions that rarely exist in nature. Which metal will become anode

and which other become cathode due to galvanic effect is relevant to the electrode

potential of the metals in the solution.

Electrode potential of a metal changes with respect to sort of ion in and

concentration of solution. For this reason electrode potential of same metals are

different in different solutions.

E E RTnF

Lnaoi= −

Here;

Eo : Standard electrode potential

ai : Activity of the metal ions in solution.




Page 20 of 146

EN ISO 9001:2000

R : Gas coefficient

F : Faraday coefficient

n : The number of the electrons in reaction

T : Temperature Standard electrode potential is the measured potential when the metal is in a

solution whose activity is 1 under 250 condition. Nernst Series can be obtained by

ordering electrode potential measured with respect to hydrogen reference electrode.

(Diagram. 1)

Diagram-1: Nernst Series ELECTROMOTOR FORCE SERIES OF THE METALS (*) Metal Reaction of

Electrode Standard Electrode Potentials, mV

Pothassium K+ + e- ⇔ K -2920 Calcium Ca+2 +2e- ⇔ Ca -2870 Sodium Na+ + e- ⇔ Na -2710 Magnesium Mg+2 + 2e- ⇔ Mg -2340 Aluminum Al+3 + 3e- ⇔ Al -1670 Manganese Mn+2 + 2e- ⇔ Mn -1050 Zinc Zn+2 + 2e- ⇔ Zn -760 Chrome Cr+3 + 3e- ⇔ Cr -710 Iron Fe+2 + 2e- ⇔ Fe -440 Cadmium Cd+2 + 2e- ⇔ Cd -400 Indium šn+2 + 2e- ⇔ šn -340 Cobalt Co+2 + 2e- ⇔ Co -277 Nickel Ni+2 + 2e- ⇔ Ni -250 Tin Sn+2 + 2e- ⇔ Sn -136 Lead Pb+2 + 2e- ⇔ Pb -126 Hydrogen 2H+ + 2e- ⇔ H2 0 Copper Cu+2 + 2e- ⇔ Cu 337 Mercury Hg+2 + 2e- ⇔ Hg 799 Silver Ag+ + e- ⇔ Ag 800 Platinum Pt+2 + 2e- ⇔ Pt 120 Gold Au+3 + 3e- ⇔ Au 1420

(*) Standard electrode potential is the potential measured in 1 molar of the solution, under 25 0 C, in equilibrium. Hydrogen is used as reference electrode and the potential of this reference electrode is considered zero. In Nernst series highest active metals are put to the top of the list. Downwards activity of the metals decreases. The metal at the top of the list becomes anode of the following metals. For




Page 21 of 146

EN ISO 9001:2000

instance Magnesium, Aluminum and Zinc metals can be used to protect the iron metal cathodically.

Fe²(rust)

Anode(Steel)

Elektrolyte(Water)

Current flowCathode (brokenmill scale )

Figure 2: Mill scale is cathodic to steel, established a corrosion cell Electrode Potential of In Soil. Electrodes potential given in Nernst series are in standards. The potential of the

metal in soil or in water is largely greater than these values. In addition, hydrogen

cannot be used as a reference electrode in practice. Instead calomel electrode or

Copper/Coppersulphate reference electrode is used. Pot values of electrode with

respect to standard hydrogen electrode are as follows:

Calomel electrode = +0.280 Volt

Copper/Coppersulphate electrode = +0,316 Volt

Saturated Copper/Coppersulphate reference electrodes used in soil. Soil potential of

various metals and alloys with respect to saturated Copper/Coppersulphate

reference electrode are shown in Diagram 2. Electromotor Force of galvanic cell as

a result of the contact between diverse metals in soil should be evaluated and thus

according to this anode-cathode should be determined, considering the potential

given in Diagram 2.




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EN ISO 9001:2000

Diagram-2: Electrode potential of various metal and alloy in soil (With respect to saturated Cu/CuSO4 electrode)

Metal or Alloy Electrode Potential, Volt (*) Magnesium (Pure) -1,75 Magnesium AZ-63 -1,60 Zinc (pure) -1,10 Aluminum (% 5 Zn) -1,05 Aluminum (Pure) -0,80 Iron (Cast) -0,50 Soft steel (clear) -0,50-0,80 Soft steel (rust) -0,20-0,50 Lead -0,50 Copper -0,20 Brass -0,20 Bronze -0,20 Carbon, Graphite, Coke +0,30

Electrode should be put as close as possible to the metal when electrode potential is

measured in soil. Otherwise it is possible to get a false value due to ohmic

resistance.

Differences in soil conditions, such as moisture content and resistivity, commonly are

responsible for creating Anodic and cathodic areas. Where there is a difference in

the concentration of oxygen in the water or in moist soils in contact with metal at

different areas, cathodes will develop at points of relatively high oxygen

concentrations and anodes at points of low concentrations. Strained portions of

metals reportedly tend to be Anodic and unstirred portions cathodic. Thus, under all

ordinary circumstances where iron and steel are exposed to natural environments,

the basic conditions essential to corrosion are present to a greater or less degree.

Figure 3

(*) Neutral Potential in Soil




Page 23 of 146

EN ISO 9001:2000

O2 O2

O2O2

Cathodic area(steelat top of pipe)

Buried pipe

Anodic area(steel at bottom of pipe)

Oxygen diffusing into earth fromground surface

Electrolyte 1(soil with ground water high in oxygen content )

Current flow

Electrolyte 2 (soil with ground water deficient in oxygen content)

Fe²(Rust) Figure-3: Metal pipe buried in moist soil may corrode on the bottom .A difference in

oxygen content at different levels in the electrolyte will produce a difference of

potential.

Thus Anodic and cathodic areas will develop, and a corrosion cell, called a

concentrations cell, will form

Pitting deserved special mention because it is the type of local call corrosion that is

predominantly responsible for the functional failure of iron and steel hydraulic

structures. Pitting may result in the perforation of water pipe, rendering it

unserviceable, even though less than %5 of the total metal has been lost through

rusting. Even where confinement of water is not a factor, pitting will cause structural

failure from localized weakening effect while there is still considerable sound metal

remaining.

Pitting develops when the Anodic (corroding) area is small in relation to the cathodic

(protected) area. For example, it can be expected where large areas of the surface

are generally covered by mill scale, applied coatings, or deposits of various kinds,

but breaks exist in the continuity of the protective materials. Pitting may also develop

on bare, clean metal surfaces because of irregularities in the physical or chemical

structure of the metal. Localized, dissimilar soil conditions at the surface of steel can

also create conditions that promote the pitting type of corrosions




Page 24 of 146

EN ISO 9001:2000

On surface containing mill scale, the total metal loss is nearly constant as the anode

area is decreased, but the degree of penetration increases. Figure 2 shows

diagrammatically how a pit forms where a break occurs in mill scale. When contact

between dissimilar materials is unavoidable and the surface is painted, it is important

to paint both materials-especially the cathode. If the anode only is coated, any weak

points such as pinholes at holidays in the coating will probably result in intense

pitting.

Severe corrosion, leading to pitting, is often caused by concentration cells;

particularly in cases in which differences in dissolved oxygen concentration occur.

When a part of the metal is in contact with water relatively low in dissolved oxygen, it

is Anodic to adjoining areas in contact with water in dissolved oxygen. This lack of

oxygen may be caused by exhaustion of dissolved oxygen in a crevice (See Fig-4)

the low-oxygen area is always Anodic. Figure-4 illustrates another type of

concentration cell; this cell at the mouth of crevice is due to a difference in

concentration of the metal in solution. These two effects sometimes blend together

as in a reentrant angle in a riveted seam.

Low Metal ÝonConcentration

METAL ION CONCENTRATION CELL

High Metal ÝonConcentration

OXYGEN CONCENTRATION CELL

High oxygenConcentration

Low OxygenConcentration

Figure-4: Corrosion caused at crevices by concentration cells; the attacks may

occur simultaneously.




Page 25 of 146

EN ISO 9001:2000

THE CORROSION OF STEEL IN CONCRETE Concrete is one of the most important construction materials. It is also a compact

material against external effects physically and chemically. In order to improve the

strength of concrete, steel rods are used in construction. However construction rods

made of soft steel. This steel can be corroded in atmosphere and in water easily.

This is because of high alkalinity of concrete. But the oxygen cannot permeate

through the concrete block by ease.

Concrete, originally, consists of agrega, segment and water. The main binding

chemical reaction takes place between water and clinker compounds of segment.

Clinker compounds form calcium silicate hydrates and calcium aluminates hydrides

by reacting with water. These hydride compounds become compact in time being

crystallized.

While clinker compounds are reacting with water, calcium hydroxide is formed by

hydrolyze of silicate. This hydroxide, which has a strong basic characteristic,

remains at solution-phase after concrete becomes compact. As a result of this pH

degree of fresh concrete, with the effect of alkali oxides in clinker compounds,

increases to 12,5 like lime solution. As concrete becomes older in time pH

decreases as a result of permeation of atmospheric carbon dioxide through concrete

body. However even in old concrete pH degree is not too low.

The high degree of concrete pH causes ℘Fe2O3 film formation on the surfaces of

steel and passivation of metal in the concrete in a short time. In an ordinary concrete

this oxide film prevents corrosion of steel without failure for along time.

Many concrete structures in industrial environments with the external effects (sea

water, some salts used to prevent ice formation, fertile wastes, etc.) becomes ugly**

The chloride ions, present in concrete construction, causes deformation of passive

** Chlorine can permeate through the concrete to structure by means at same concrete ingredient used for accelerating of concreting




Page 26 of 146

EN ISO 9001:2000

oxide film formation on the steel surfaces. In these conditions construction rods can

be corroded severely. It is appropriate condition the presence of chloride over 0,7-

1,2 Kg in unit volume (1 m3) for the remain of corrosion.

The result of corrosion in concrete is not only the loss of steel but also cracking and

the concrete blocks because the volume of the chemical compounds (rust), which

appears on steel rods, is greater respectively.

There is no an effective mean to repair the old concrete blocks due to corrosion.

However, However if it is not cracked by corrosion yet, these repair methods are

recommended as follows:

The upper plate of the concrete above rods is removed and rods are substituted by

new ones then it is reconcreted.

The upper plate of the concrete above rods is removed and then it is recovered by

concrete asphalt or epoxy concrete.

If physical properties of the structure is appropriate and if in 1m3 of concrete 1,2 Kg

chloride are present then a new 7,5 cm-thick concrete plate should be put on the top

without removing rods and concrete.

It may be possible to keep the structure erect for a certain period of time with one of

these methods. Nevertheless here the goal is to protect the structure, not to repair it

before corrosion effect.

In order to prevent corrosion:

Appropriate design

Appropriate material selection

Sufficient coating

Cathodic Protection

Anodic protection




Page 27 of 146

EN ISO 9001:2000

should be provided. The items except for cathodic protection are ones that decrease

corrosion rate in other words prevent partially. Cathodic Protection is rather effective,

protective entire method.

CATHODIC PROTECTION Cathodic Protection is a major factor in corrosion control of metals. When an

external electric current is applied, the corrosion rate can be reduced to practically

zero. Under these conditions the metal can remain in a corrosive environment

indefinitely without deterioration.

In practice, cathodic protection can be utilized with such metals as steel, copper,

brass, lead, and aluminum against corrosion in all soils and almost all aqueous

media. Although it cannot be used above the waterline (since theme impressed

electric current cannot reach areas out of the electrolyte) it can be effectively used to

eliminate corrosion fatigue, intergranuler corrosion, stress corrosion cracking,

dezincification of brass, or pitting of stainless steels in sea water or steel in soil.

In 1982, Sir Humphrey Davy, reported that by coupling iron or zinc to copper, the

copper could be protected against corrosion. The British admiralty had blocks of

attached to the hulls of copper sheathed vessels to provide cathodic protection.

Unfortunately, cathodically protected copper is subject to fouling by marine life,

which reduced the speed of vessels under sail and forced the admiralty to

discontinue the practice. However, the corrosion rate of the copper had been

appreciably reduced. Unprotected copper supplies are sufficient number of copper

ions to poison fouling organisms.

In 1829, Edmund Davy was successful in protecting the iron portions of buoys by

using zinc block, and in 1840, Robert Mallet produced a zinc allot that was

particularly suited as a sacrificial anode. The fitting of zinc slabs to the steel hulls of

vessels became standard practice as wooden hulls were replaced. This provided

localized protection specifically against the galvanic action of a




Page 28 of 146

EN ISO 9001:2000

Bronze propeller. Overall protection of seagoing vessels was not investigated again

until 1950, when the Canadian Navy determined that the proper use of antifouling

paints in conjunction with corrosion-resistant paints made cathodic protection of

ships feasible and could reduce maintenance costs.

About 1910-1912 the first application of cathodic protection by means of an

impressed electrical current was undertaken in England and the United States.

Since that time the general use of cathodic protection has spread widely. There are

thousands of miles of buried pipelines and cables, which are protected in this

manner.

This form of protection is also used for water tanks, submarines, canal gates marine

piling, condensers, and chemical equipment.

THEORY

The basis of cathodic protection is shown in the polarizing diagram for a Cu-Zn cell,

Fig. 1. If polarization of the cathode is continued by use of an external current

beyond the corrosion potential to the open-circuit potential of the anode, both

electrodes reach the same potential and no corrosion of the zinc can take place.

The corrosion rate will remain at zero if the metal is polarized slightly beyond the

open-circuit potential FA of the anode. However this excess current has no value and

may be injurious to amphoteric metals or coatings. For this reason in actual practice

the impressed current is maintained close to the theoretical minimum.




Page 29 of 146

EN ISO 9001:2000

CURRENT

I R(max) e

Φ

Φ

Φ

Cu

(kor.)

Zn

I(max) Figure 5: Polarization of copper -zinc cell

CORRODING METAL

AUXILIARYANODE

-

+

+

ELECTROLYTE

+-

B

Figure .6: Cathodic Protection using impressed current on local action cell




Page 30 of 146

EN ISO 9001:2000

If the current falls below that required for complete protection, protection will still be

afforded. There are some criteria for complete protection of the steel and iron

structures as follow:

Potential value, measured at each point of the metal, should be -850 mV or more

negative than -850 mV with respect to Cu/CuSO4 reference electrode.

A 100 mV decrease of potential is sufficient when current is applied to steel

structures.

Polarization of the steel structure to -300 mV with respect to the natural potential

without applying current.

There are two types of cathodic protection: Impressed current cathodic protection

Galvanic anode cathodic protection




Page 31 of 146

EN ISO 9001:2000

IMPRESSED CURRENT CATHODIC PROTECTION

In order to apply cathodic protection, a direct current supply and an auxiliary anode

are needed. This auxiliary anode usually is made of graphite, iron, or have recently

improved titanium materials and is put little away from the structure to be protected.

Anode is connected to positive, structure to negative pole. This allows the current

flow to structure through the electrolyte. Applied voltages are not critical values as

far as it provides sufficient current density to all parts of the structure. The resistivity

of soil defines voltages to be applied.

GALVANIC ANODE CATHODIC PROTECTION

In this system a more active metal than the metal to be protected in galvanic series

is used as an anode. A galvanic cell is established in the current direction as

defined. Magnesium, Aluminum, Zinc and their alloys are used as being galvanic

anode. Because these anodes are portable electricity supply they are used in the

places where is absent or where the cost of furnishing electricity cables to the field.

In US structures are mostly protected by Magnesium anodes. For this reason nearly

10 millions pound magnesium are consumed. Open-circuit potential difference

between magnesium and steel is approx. 1 volt. This means one anode can protect

a certain length of pipeline.




Page 32 of 146

EN ISO 9001:2000

Anode Requirement

The current, necessary to protect a 1m2 surface is called anode requirement of

cathodic protection. The dimension, life expectancy and the number of anodes can

be pointed out by calculations. Some of the electrochemical properties of common

metals to be used as galvanic anode, magnesium, zinc and aluminum are given in

the following table:

Metal Theoretical current capacity, A.hr/lb

Anodic efficiency, %

Practical current capacity A.hr/lb

Magnesium 1000 50 500

Zinc 370 90 333

Aluminum 1345 60 810

Usage With Coatings

Using isolative coating is always an advantage. Such coating is effective in

distributing current, reducing total current requirement and in prolonging life span of

an anode. For example in a coated pipeline, distribution of current is more uniform,

numbers of anodes and the total current requirement is fewer than in bare pipelines.

One anode can protect a longer part of pipe for longer time.

Potential Measurements Protection degree is obtained measuring potential of the structure to be protected

quantitatively. This depends on the concept that cathodic protection is complete

when local action cells of the structure are polarized to open-circuit Anodic potential.

In order to realize this measurement reference electrode should be put as close as

possible to the structure to abandon or minimize the mistakes caused by ohmic

decrease. For the buried pipes a place should be selected in the way of pipe above

the ground level.




Page 33 of 146

EN ISO 9001:2000

To determine whether the metal is protected or not it is necessary to look at the

potential values of electrodes to be sure whether they provide these values.

Reference Electrode Protection Potential, mV

Saturated calomel Electrode, Hg2 Cl2 -0,780

Silver-Silver Chloride, (Ag/AgCl) -0,810

Copper-Coppersulphate (Cu/CuSO4) -0,850

Zinc +0,250

OVERPROTECTION

Overprotection of the steel structures, to a moderate degree, usually does not cause

any problems. The primary disadvantages are waste of electric power and increased

consumption of auxiliary anodes. When the overprotection is excessive, hydrogen

can be generated at the protected structure in sufficient quantities to cause blistering

of organic coating, hydrogen embitterment of the steel, or hydrogen cracking.

Damage to steel by hydrogen absorption is more prevalent in environments where

sulfides are present.




Page 34 of 146

EN ISO 9001:2000

CATHODIC PROTECTION AGAINST CORROSION IN CONCRETE In recent years cathodic protection of Ferro Crete rods has been involved in cathodic

protection field. Ferro Crete rods can be protected both cathodically and with

impressed current protection system.

The most essential condition for cathodic protection in concrete is that connections of Ferro Crete rods should be perfect. Normally rods are in contact with each other but this is not sufficient for low voltage electric current. It is better to weld rods to each other.

Cathodic Protection Criteria

In normal conditions for a perfect protection of steel structure it should be polarized

cathodically more electronegative than -0,85 V with respect to saturated Cu/Cu

(SO4) 2 reference electrode. This value correspond -0,80 Volts with Ag/AgCl

reference electrode. In cathodic protection system in concrete it is impossible to

reach at this value due to passivity. For cathodic protection of steel in concrete

another criterion should be considered. It is sufficient for protection of steel a

polarization variation of 100 mV.




Page 35 of 146

EN ISO 9001:2000

Application Cathodic Protection

An uniform current distribution is necessary for the application of cathodic protection

to Ferro Crete rods. For this reason the anode shape and size is very important. The

most appropriate method is using oxide coated titanium anodes in cage shape.

REFERENCE ELECTRODES 1-Standard Hydrogen Electrode, (Pt/H2/H+) Electrode reaction 2H+ + 2e- ⇔ H2 (H+) = 1 PH2 = 1 atm E= 0 mV 2-Calomel Electrode, (Hg/Hg2Cl2, Cl) Electrode reaction Hg2Cl2 + 2e- ⇔ 2Hg + 2Cl- E=0.2677-0.059 log aCl_ E= 244 V ( saturated chlorine) 3-Silver-Silver Chlorine ,(Ag/AgCl - ) Electrode reaction AgCl + 2e- ⇔ Ag + Cl- E=0,2224-0,059 log aCl E= 250 V (Sea water ) 4-Copper/Copper sulfate,(Cu/SO 4 ,Cu +2 ) Electrode reaction Cu+2 + 2e- ⇔ Cu E=0,340+0,0259 log a Cu +2 E= 318 V (Saturated CuSO4) 5-Zinc/Sea water E= 800 mV




Page 36 of 146

EN ISO 9001:2000

SECTION -5

OOOUUURRR AAACCCTTTIIIVVVIIITTTYYY FFFIIIEEELLLDDDSSS OOOFFF CCCAAATTTHHHOOODDDIIICCC PPPRRROOOTTTEEECCCTTTIIIOOONNN

ErgilCorrosion is a registered trademark of Ergil Group

Head Office:M.Nezihi Ozmen Mah.Fatih Cad.Kayikci Sk.No.8 K:2 Merter-ISTANBUL /TURKEY Phone: +90 212 643 62 26 (Pbx) Fax: +90 212 643 62 22

Dubai Office:Rak Free Trade Zone P.O.Box:10559 Ras Al Khamiah U.A.E Factory:Atatürk Cad.OSB.Fatih Sitesi 6/a Blok Ikitelli-ISTANBUL/TURKEY

www.ergilgroup.com [email protected]

EN ISO 9001:2000

CATHODIC PROTECTION

DESIGN SERVıCE

o FRONT DESIGN WORKS o DESIGN CALCULATION o SPECIFICATIONS AND DESCRIPTIONS o DETAILED CURRENT NECCESSITY TESTS

SOLUTION OF A PROBLEM UPKEEP AND REPAIR MONTAGE COUNSELING UNDERTAKING

CORROSION CONTROL PROGRAMME CONTROL SYSTEM FROM FAR ANNUAL CONTROLS PLACE REPORTS DATA ANALYSIS WITH COMPUTER RECORDING AND PROCESSING EDUCATION PROGRAMS FEASIBILITY ACTIVITIES COATING CONTACTS AND SPECIFICATIONS CONTROLLER OF CATHODIC PROTECTION

CORROSION-INSTALLATION Rehabilitation Systems of Pipelines Splash Zone Protection Systems Turn Key Cathodic Protection, Projection, Installation, Undertaking, and Maintenance Programs

• galvanic anodes • mağnesium anodes

D profile Mg anodes with high potatial H-1 casting Magnesium anodes Rod and ribbon type anodes Service anodes

• aluminium anod quay platform anodes pipe line handcuffs anodes ship anodes

• zinc anod ship anodes





EN ISO 9001:2000

pipe line handcuffs anodes zinc ribbon anod Petrol tanks floor anodesı

• kondenser /heat changer anod

Magnesium anodes zinc anodes

• special anodes

runaway current drainage anodes Static elektric drainage anodes Special anodes

• galvanic anod filling materials TS-5141 A type anode filling material TS-5141 B type anode filling material Special aim filling material

• Outer current welded system anodes Grafit anodes İron silicone anodes Mixed metal oxide covered Ti anodes Tube anodes rod anodes wire anodes Plaque anodes sieve anodes Profile anodes Probe (pipe in) anode Special aim anodes Underground storage tanks anodesı Tank anodes Tank outer anodes Platinium Anodes Platiniumed Ti anodes silver-lead Antimuan anodes water tanks & Kondenser anodes

• anode accessories Epoxy Cap Compressed Cap by Heat Deep Well Centering Equipment Anode Sting Stabilizing Equipment





EN ISO 9001:2000

ANODE FILLING MATERIAL

Calcined Petroleum-coke Metallurgic Coke Loresco™ Filling Material

• cable NYY HMWPE HALAR KYNAR

EPR/CSPE TRANSFORMER RECTIFIER (T/R) UNITS

Iller Bankasi Type Air-cooler T/R Units Iller Bankasi Type Oil-cooler T/R Units SCADA Fitted Type Air-cooler T/R Units SCADA Fitted Type Oil-cooler T/R Units PC 486 Microprocessor Based Type Air-cooler T/R Units PC 486 Microprocessor Based Type Oil-cooler T/R Units Photovoltaic Systems

T/R UNITS SPECIAL ACCESSORIES

Polarization Cells Insulator and Spark-gap

REFERENCE ELECTRODES

Portable and stable Type Cu/CuSO4,Ag/AgCl 3K (Domestic manufacture) TINKER & RASOR MC MILLER COLE-PARMER PROCOR CPS HARCO

( Other Type reference electrodes/Calomel, Zn )





EN ISO 9001:2000

CASING EQUIPMENT

Monolithic Insulation Connection Flange Insulation joints & Insulation Connection Casing Insulators Flange Protective Casings Casing Caps

CATHODIC PROTECTION TEST AND MEASUREMENT STATIONS

TS-5141 Piped Measurement Boxes TS-5141 NATO Type Measurement Boxes BOTAŞ Type Measurement Boxes Manual Type For Special Use

CATHODIC PROTECTION CONTROL INSTRUMENTS

• Portable Holiday Detectors • Avometre (High Resistance) • Pipe and Cable Detectors • Soil Resistivity Instruments • Measurement Instruments Related to Coating • pH-meter Instruments • Saltmeter • COATING MATERIALS and COATING EQUIPMENT • Pipe Coating Bands and Primers • TapeCoat® • Tek-Rap ® • 3M Scotchrap • Termo Weld Materials • CORROSION and CATHODIC PROTECTION of MARINE

STRUCTURES • Platform & Corrosion Monitoring of Pipelines • Corrosion Monitoring, Projection, Installation, Undertaking and

Controlling of Cathodic Protection of Jetty and Marine Pile Structures

• • CATHODIC PROTECTION SYSTEM of WATER & SEWERAGE

WATER





EN ISO 9001:2000

• Cathodic Protection Systems of Water Pipelines • Cathodic Protection Systems of Water Tanks • Cathodic Protection Systems of Water Works • CATHODIC PROTECTION of PETROLEUM PLANTS • Cathodic Protection System of Fuel Oil Pipeline • Cathodic Protection System of Underground and Storage Tanks • CATHODIC PROTECTION of NATURALGAS PLANTS • Cathodic Protection Systems of Natural gas Pipelines • Cathodic Protection Systems of RMS Stations • Cathodic Protection Systems of Underground Storage Tanks • Cathodic Protection Systems of Natural gas Distribution

Pipelines • STEEL STRUCTURES IN CONCRETE • Cathodic Protection System of Reinforced Cored Steel • Cathodic Protection System of Dam Pipes

• Cathodic Protection System of Steel Structures of In Jetty

Concrete Platform

• Cathodic Protection System of Bridge Suspension Bridge • Cathodic Protection System of Structures in Concrete • Cathodic Protection System of Base Steel Structures • Cathodic Protection System of Underground Tunnels.

TESTS

Soil Tests ∗ Soil Resistivity Measurement and Calculations ∗ Reduction Potential Measurement and Calculations ∗ pH Measurement and Calculations ∗ Salt Measurement and Calculations ∗ Moist Measurement and Calculations ∗ Other Soil Analysis

Electrical continuity and resistance tests Measuring Rate and Sort of Corrosion Insulation Tests Potential Measurements





EN ISO 9001:2000

Polarization Cells

Low Resistance Grounding E-logi Tests Potential Drop Monitoring IR Drop Monitoring Stray Current Tests

INSTALLATION

Rehabilitation Systems of Pipelines Splash Zone Protection Systems Turn Key Cathodic Protection, Projection, Installation, Undertaking, and Maintenance Programs




Page 39 of 146

EN ISO 9001:2000

TRANSFORMER RECTIFIER (T/R) UNITS

SCADA Fitted Type Air-cooler T/R Units SCADA Fitted Type Oil-cooler T/R Units PC 486 Microprocessor Based Type Air-cooler T/R Units PC 486 Microprocessor Based Type Oil-cooler T/R Units Photovoltaic Systems

T/R UNITS SPECIAL ACCESSORIES Polarization Cells Insulator and Spark-gap

REFERENCE ELECTRODES Portable and stable Type Cu/CuSO4,Ag/AgCl

Ergil (Domestic manufacture) TINKER & RASOR MC MILLER COLE-PARMER PROCOR CPS HARCO

( Other Type reference electrodes/Calomel, Zn ) CASING EQUIPMENT

Monolithic Insulation Connection Flange Insulation joints & Insulation Connection Casing Insulators Flange Protective Casings Casing Caps

CATHODIC PROTECTION TEST AND MEASUREMENT STATIONS TS-5141 Piped Measurement Boxes TS-5141 NATO Type Measurement Boxes BOTAŞ Type Measurement Boxes Manual Type For Special Use

CATHODIC PROTECTION CONTROL INSTRUMENTS Portable Holiday Detectors Avometre (High Resistance) Pipe and Cable Detectors Soil Resistivity Instruments Measurement Instruments Related to Coating pH-meter Instruments

• Saltmeter • COATING MATERIALS and COATING EQUIPMENT

Pipe Coating Bands and Primers TapeCoat® Tek-Rap ® 3M Scotchrap Termo Weld Materials

• CORROSION and CATHODIC PROTECTION of MARINE STRUCTURES • Platform & Corrosion Monitoring of Pipelines




Page 40 of 146

EN ISO 9001:2000

• Corrosion Monitoring, Projection, Installation, Undertaking and Controlling of Cathodic Protection of Jetty and Marine Pile Structures

• CATHODIC PROTECTION SYSTEM of WATER & SEWERAGE WATER • Cathodic Protection Systems of Water Pipelines • Cathodic Protection Systems of Water Tanks • Cathodic Protection Systems of Water Works • CATHODIC PROTECTION of PETROLEUM PLANTS • Cathodic Protection System of Fuel Oil Pipeline • Cathodic Protection System of Underground and Storage Tanks • CATHODIC PROTECTION of NATURALGAS PLANTS • Cathodic Protection Systems of Natural gas Pipelines • Cathodic Protection Systems of RMS Stations • Cathodic Protection Systems of Underground Storage Tanks • Cathodic Protection Systems of Natural gas Distribution Pipelines STEEL STRUCTURES IN CONCRETE • Cathodic Protection System of Reinforced Cored Steel • Cathodic Protection System of Dam Pipes • Cathodic Protection System of Steel Structures of In Jetty Concrete Platform • Cathodic Protection System of Bridge Suspension Bridge • Cathodic Protection System of Structures in Concrete • Cathodic Protection System of Base Steel Structures • Cathodic Protection System of Underground Tunnels. TESTS

Soil Tests ∗ Soil Resistivity Measurement and Calculations ∗ Reduction Potential Measurement and Calculations ∗ pH Measurement and Calculations ∗ Salt Measurement and Calculations ∗ Moist Measurement and Calculations ∗ Other Soil Analysis

Electrical continuity and resistance tests ç Measuring Rate and Sort of Corrosion ç Insulation Tests ç Potential Measurements

Polarization Cells ç Low Resistance Grounding ç E-logi Tests ç Potential Drop Monitoring ç IR Drop Monitoring ç Stray Current Tests

INSTALLATION ç Rehabilitation Systems of Pipelines ç Splash Zone Protection Systems ç Turn Key Cathodic Protection, Projection, Installation, Undertaking, and

Maintenance Programs




Page 41 of 146

EN ISO 9001:2000

SECTION -6

OOOUUURRR CCCAAATTTHHHOOODDDIIICCC PPPRRROOOTTTEEECCCTTTIIIOOONNN RRREEEFFFEEERRREEENNNCCCEEESSS

www.ergilmakina.com.tr 6/1

No Customer Name Of Work SCOPE PROJECT BUDGET Start Date Completion Date

1 KARADENIZ BAKIR ISLETMELERİ A.S CATHODIC PROTECTION FOR 56 km X 2 COPPER TRANSFER PIPELINE BETWEEN MURGUL FACILITIES AND HOPA

CATHODIC PROTECTION OF 56 KM PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $189.000,00 1992 1993

2 AYGAZ SUPPLY OF CATHODIC PROTECTION MATERIALS FOR AYGAZ A.S GAS FILLING PLANT SUPPLY OF CATHODIC PROTECTION MATERIALS FOR LPG TANKS $120.000,00 1992 1994

3 BILKENT SUPPLY OF CATHODIC PROTECTION MATERIALS FOR INTERNAL NATURAL GAS PIPES OF BILKENT UNIVERSITY DWELLINGS.

CATHODIC PROTECTION OF 5 KM NATURAL GAS PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $45.000,00 1993 1994

4 ILLER BANKASI SUPPLY OF CATHODIC PROTECTION MATERIALS FOR ILLER BANK DRINKING WATER DEPARTMENT TRABZON AND GIRESUN DRINKING WATER PLANT

CATHODIC PROTECTION OF 80 KM DRINKING WATER PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $150.000,00 1993 1994

5 ISDEMIR SUPPLY OF CATHODIC PROTECTION MATERIALS FOR ISDEMİR ISKENDERUN IRONAND STEEL FACTORYI, MERSIN CREEK DRAINAGE LINE

CATHODIC PROTECTION OF 8 km WATER PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $135.000,00 1993 1994

6 BOTAS – STFA CATHODIC PROTECTION FOR 210 KM LINE BETWEEN CANAKKALE CERAMIC FACTORY A.S., CAN AND BURSA

CATHODIC PROTECTION OF 210 KM NATURAL GAS PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $165.000,00 1994 1995

7 BOTAS – FERNAS CATHODIC PROTECTION FOR NATURAL GAS LINE BETWEEN CORLU AND ESENYURT – JOINT VENTURE

CATHODIC PROTECTION OF NATURAL GAS PIPE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $120.000,00 1994 1995

8 BOTAS – ENKA CATHODIC PROTECTION FOR INTERNAL PIPES OF GEBZE NATURAL GAS PRESSURE REDUCTION STATION

CATHODIC PROTECTION OF NATURAL GAS PIPE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $65.000,00 1994 1995

9 TUPRAS IZMIT RAFINERISI TUPRAS IZMIT REFINING PLANT – MANUFACTURE OF GALVANIC ANODE MANUFACTURE OF GALVANIC ANODES FOR STEEL QUAY LEGS $145.000,00 1994 1995

10 TUPRAS IZMIT RAFINERISI CATHODIC PROTECTION FOR FILLING QUAY LEGS OF TUPRAS IZMIT REFINING PLANT

CATHODIC PROTECTION OF STEEL QUAY LEGS+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $450.000,00 1994 1995

11 TUPRAS-KIRIKKALE CATHODIC PROTECTION FOR 4 OIL TANK BOTTOM IN TUPRAS KIRIKKALE REFINING PLANT CATHODIC PROTECTION OF INTERNAL PARTS OF TANKS+ENGINEERING+APPLICATION $67.000,00 1994 1995

12 TEKELSUPPLY OF CATHODIC PROTECTION MATERIALS FOR WATER DRAINAGE LINE BETWEEN THE TURKISH STATE LIQUOR AND TOBACCO MONOPOLY ALASEHIR-SOMA FACTORY AND AVSAR DAM.

CATHODIC PROTECTION OF WATER PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $123.000,00 1995 1996

13 EGO NATURAL GAS DEPARTMENT CATHODIC PROTECTION FOR VARIOUS LINES - CONSUMABLES CATHODIC PROTECTION MATERIALS $23.000,00 1995 1996

14 AFJET SUPPLY OF CATHODIC PROTECTION MATEIALS FOR AKJET AFYON GEOTHERMAL PIPE LINE

CATHODIC PROTECTION OF PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $150.000,00 1996 1997

15 BOTAS SUPPLY OF CATHODIC PROTECTION MATEIALS FOR ANADOLU UNIVERSITY NATURAL GAS PIPE LINE CATHODIC PROTECTION OF NATURAL GAS PIPE LINE $45.000,00 1996 1997

16 ISTON A.S CATHODIC PROTECTION FOR OLD GALATA BRIDGE FLOATS CATHODIC PROTECTION OF PANTOONS+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $230.000,00 1996 1997

17 TUPRAS ALIAGA RAFINERISI MANUFACTURE OF ANODES FOR CATHODIC PROTECTION, WITH GALVANIC ANODES, OF QUAY LEGS MANUFACTURE AND ASSEMBLY OF GALVANIC ANODES FOR STEEL QUAY LEGS $210.000,00 1996 1997

18 ISTON A.S CATHODIC PROTECTION FOR KARAKOY FLOAT CATHODIC PROTECTION OF PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $180.000,00 1996 1997

19 ISTON A.S CATHODIC PROTECTION FOR UNKAPANI BRIDGE FLOATS CATHODIC PROTECTION OF PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $156.000,00 1996 1997

20 Iski(Istanbul Ve Kanalizasyon Idaresi(TEKFEN INSAAT)

CATHODIC PROTECTION FOR Ø 800, Ø 900 mm STEEL PIPELINE OF 1ST STAGE OF UYDUKENT (SATTELLITE CITY) PROJECT

CATHODIC PROTECTION OF WATER PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $123.000,00 1996 1997

OUR CATHODIC PROTECTION REFERENCES

EN ISO 9001:2000

Adres: Atatürk Caddesi Organize Sanayii bölgesi. Fatih Sitesi 6/A 34670 Blok –İKİTELLİ_İSTANBULTel: 0212 485 40 07 Faks: 0 212 485 40 42



21 IGDAS-2000 CATHODIC PROTECTION OF NATURAL GAS PIPE LINE (FOR 5 MAJOR LINES) CATHODIC PROTECTION OF NATURAL GAS PIPE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $123.000,00 1998 1999

22 Iski(Istanbul Ve Kanalizasyon Idaresi(ZITAS) CATHODIC PROTECTION FOR ELMALI-ÜSKÜDAR LINE CATHODIC PROTECTION OF WATER CONDULT PIPE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $189.000,00 1998 1999

23 TPAO SUPPLY OF CATHODIC PROTECTION MATERIALS FOR 76 KM AND 8 “ PIPE LINE BETWEEN TPAO DEGIRMENKOY AND TRAKYA CAM FACTORY CATHODIC PROTECTION OF NATURAL GAS PIPE+ENGINEERING+SUPPLY OF MATERIALS $98.000,00 1998 1999

24 Iski(Istanbul Ve Kanalizasyon Idaresi COMPLETE CATHODIC PROTECTION FOR 3. STEP ASIA – EUROPE – JOINT VENTURE

CATHODIC PROTECTION OF WATER CONDULT PIPE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $890.000,00 1998 2001

25 Iski(Istanbul Ve Kanalizasyon Idaresi CATHODIC PROTECTION FOR STEEL CLEAN WATER PIPE LINE, ASIAN SIDE, 5. STEP 2. SECTION

CATHODIC PROTECTION OF WATER CONDULT PIPE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $1.450.000,00 1998 2001

26 Iski(Istanbul Ve Kanalizasyon Idaresi(AHMET ASLAN)

CATHODIC PROTECTION FOR DRAINAGE LINE BETWEEN KAGITHANE MUNZEVI AND SILAHTAR


27 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION FOR FUEL STORAGE TANK BOTTOMS(ALİAGA) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $25.000,00 1999 2000

28 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION FOR FUEL STORAGE TANK BOTTOMS(ALİAGA) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $18.000,00 1999 2000

29 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION FOR FUEL STORAGE TANK BOTTOMS(IZMIT) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $33.000,00 1999 2000

30 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION FOR FUEL STORAGE TANK BOTTOMS(IZMIT) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $33.000,00 1999 2000

31 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION FOR FUEL TANK BOTTOMS(MERSIN) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $33.000,00 1999 2000

32 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION FOR FUEL TANK BOTTOMS(MERSIN) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $28.000,00 1999 2000

33 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION OF LAND AND UNDERWATER FUEL PIPE LINE ALİAGA CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $45.000,00 1999 2000

34 OPET PETROLCÜLÜK A.S CATHODIC PROTECTION OF LAND AND UNDERWATER FUEL PIPE LINE IZMIT CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $38.000,00 1999 2000

35 Iski(Istanbul Ve Kanalizasyon Idaresi(MEHMET CAKAR INSAAT) CATHODIC PROTECTION FOR SULTANBEYLI DISTRIBUTING LINE CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF

MATERIALS+APPLICATION $67.000,00 1999 2000

36 Iski(Istanbul Ve Kanalizasyon Idaresi(AHMET ASLAN) Kagithane Munzevi – Silahtar Arası Cathodic Protection of Condult Line CATHODIC PROTECTION OF WATER CONDULT PIPE+ENGINEERING+SUPPLY OF


37 Iski(Istanbul Ve Kanalizasyon Idaresi)(Kalyon Insaat) CATHODIC PROTECTION FOR KEMERBURGAZ DRAINAGE LINE CATHODIC PROTECTION OF WATER CONDULT PIPE+ENGINEERING+SUPPLY OF


38 Iski(Istanbul Ve Kanalizasyon Idaresi)(Kalyon Insaat)

CATHODIC PROTECTION FOR DRAINAGE LINE BETWEEN MALKOcOgLU AND BASAKSEHIR, IKITELLI


39 Iski(Istanbul Ve Kanalizasyon Idaresi)(Çiğdem İnşaat)

CATHODIC PROTECTION FOR Ø 1600 DRAINAGE LINE SUPPLEMENT BETWEEN OMERLI AND TUZLA, AND M4-M5-L1 CONDUCTION LINE


OUR REFERENCES CATHODIC PROTECTIONEN ISO 9001:2000




40 Iski(Istanbul Ve Kanalizasyon Idaresi)(Çiğdem İnşaat)

CATHODIC PROTECTION FOR Ø 1600 DRAINAGE LINE BETWEEN DUDULLU AND KOZYATAGI


41 Iski(Istanbul Ve Kanalizasyon Idaresi)(Kalyon Insaat)

CATHODIC PROTECTION FOR Ø 2200 DRAINAGE LINE BETWEEN OMERLİ AND CAMLICA


42 Iski(Istanbul Ve Kanalizasyon Idaresi)(Eren Insaat)

CATHODIC PROTECTION FOR Ø 2200 DRAINAGE LINE BETWEEN OMERLI AND TUZLA


43 DDY ISKENDERUN LIMAN ISLETMELERI CATHODIC PROTECTION OF MAIN QUAY LEGS CATHODIC PROTECTION OF WATER CONDULT PIPE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $106.000,00 2000 2001

44 Iski(Istanbul Ve Kanalizasyon Idaresi) CATHODIC PROTECTION FOR DIRECT DRAINAGE LINE BETWEEN KARTAL MAIN TANK-SOGANLIK MAIN TANK

CATHODIC PROTECTION(WITH EXTERNAL CURRENT SOURCE) OF STEEL QUAY LEGS+ENGINEERING+SUPPLY OF MATERIALS+COMMISSIONING $79.000,00 2000 2001

45 ALTINBAŞ PETROL A.S – CATHODIC PROTECTION FOR FUEL STORAGE TANK BOTTOMS IN KORFEZ FILLING PLANT


46 ALTINBAŞ PETROL A.S – CATHODIC PROTECTION FOR FUEL STORAGE TANK BOTTOMS IN MERSiN FILLING PLANT CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $24.500,00 2000 2001

47 POAS GENEL MUDURLUGU CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF ALİAGA PLANT CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $28.000,00 2001 2002

48 POAS GENEL MUDURLUGU CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF ALİAGA PLANT (WITH GALVANIC ANODES)

CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $67.000,00 2001 2002

49 POAŞ GENEL MÜDÜRLÜĞÜ CATHODIC PROTECTION UNDERWATER PIPELINES OF ALİAGA PLANT CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $28.000,00 2001 2002

50 POAS GENEL MUDURLUGU CATHODIC PROTECTION FOR UNDERWATER PIPELINE SLANK CARRIAGE BUOYS CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $78.000,00 2001 2002

51 POAS GENEL MUDURLUGU-HARAMIDERE CATHODIC PROTECTION OF PIPE LINE BETWEEN HARAMIDERE AND ESENKENT CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $88.000,00 2001 2002

52 POAS GENEL MUDURLUGU-HARAMIDERE CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF HARAMIDERE PLANT


53 POAS GENEL MUDURLUGU-HARAMIDERE CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF HARAMIDERE PLANT (WITH GALVANIC ANODES)


54 POAS GENEL MUDURLUGU-HARAMIDERE CATHODIC PROTECTION UNDERWATER PIPELINES OF HARAMIDERE PLANT CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $65.000,00 2001 2002

55 POAS GENEL MUDURLUGU-ISKENDERUN CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF ISKENDERUN PLANT


56 POAS GENEL MUDURLUGU-ISKENDERUN CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF İSKENDERUN PLANT (WITH GALVANIC ANODES)


57 POAS GENEL MUDURLUGU-ISKENDERUN CATHODIC PROTECTION UNDERWATER PIPELINES OF ISKENDERUN PLANT CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $37.800,00 2001 2002

58 POAS GENEL MUDURLUGU(KORFEZ) CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF KÖRFEZ PLANT


59 POAS GENEL MUDURLUGU(KORFEZ) CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF KÖRFEZ PLANT (WITH GALVANIC ANODES)


OUR REFERENCES CATHODIC PROTECTION




No Customer Name Of Work SCOPE PROJECT BUDGET Start Date Completion D t

60 POAŞ GENEL MUDURLUGU(KORFEZ) CATHODIC PROTECTION UNDERWATER PIPELINES OF KÖRFEZ PLANT CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $64.000,00 2001 2002

61 POAS GENEL MUDURLUGU-MERSİN CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF MERSIN PLANT


62 POAS GENEL MUDURLUGU-MERSIN CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF MERSIN PLANT (WITH GALVANIC ANODES) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $18.000,00 2001 2002

63 POAS GENEL MUDURLUGU-MERSIN CATHODIC PROTECTION UNDERWATER PIPELINES OF MERSIN PLANT CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $87.000,00 2001 2002

64 POAS GENEL MUDURLUGU-MUDANYA CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF MUDANYA PLANT


65 POAS GENEL MUDURLUGU-MUDANYA CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF MUDANYA PLANT (WITH GALVANIC ANODES) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $18.000,00 2001 2002

66 POAS GENEL MUDURLUGU-MUDANYA CATHODIC PROTECTION UNDERWATER PIPELINES OF MUDANYA PLANT CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $87.000,00 2001 2002

67 POAS GENEL MUDURLUGU CATHODIC PROTECTION FOR 7X8” FUEL PIPELINE BETWEEN PETROL OFISI AND TUPRAS REFINING PLANT


68 POAS GENEL MUDURLUGU-SAMSUN CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF SAMSUN PLANT


69 POAS GENEL MUDURLUGU-SAMSUN CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF SAMSUN PLANT (WITH GALVANIC ANODES) CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $18.000,00 2001 2002

70 POAS GENEL MUDURLUGU-SAMSUN CATHODIC PROTECTION UNDERWATER PIPELINES OF SAMSUN PLANT CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $87.000,00 2001 2002

71 POAS GENEL MUDURLUGU-TRABZON CATHODIC PROTECTION FOR FUEL PIPES AND QUENCHING WATER HYDRANT PIPES OF TRABZON PLANT


72 POAS GENEL MUDURLUGU-TRABZON CATHODIC PROTECTION FOR INNER BOTTOMS OF FUEL TANKS OF TRABZON PLANT (WITH GALVANIC ANODES)


73 POAS GENEL MUDURLUGU-TRABZON CATHODIC PROTECTION UNDERWATER PIPELINES OF TRABZON PLANT CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $87.000,00 2001 2002

74 ATAKOY HOTELS CATHODIC PROTECTION OF NATURAL GAS PIPE LINE CATHODIC PROTECTION OF NATURAL GAS PIPE LINE $6.000,00 2002 2002

75 BOTAS ANKARA REGIONAL MANAGEMENT SUPPLY OF MIXED METAL OXIDE COATED ANODE AND REFERENCE ELECTRODE SUPPLY OF MATERIALS $45.000,00 2002 2002

76 BOTAS ANKARA REGIONAL MANAGEMENT SUPPLY OF TRANSFORMER RECTIFIER UNIT MANUFACTURE AND SUPPLY OF 10 UNITS OF T/R UNITSİ $45.000,00 2002 CONTINUING

77 BOTAS /KULAK CONSTRUCTION CATHODIC PROTECTION OF DOGUBEYAZIT COMPRESSOR STATION PIPES ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $45.000,00 2002 CONTINUING

78 TEKNOCOAT CATHODIC PROTECTION OF LPG TANKS ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $13.000,00 2002 2003

79 BSH- PROFILO CERKEZKOY FACTORIESI CATHODIC PROTECTION OF NATURAL GAS PIPE LINE ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $9.800,00 2003 2003

OUR REFERENCES CATHODIC PROTECTIONEN ISO 9001:2000




80 BOTAS-KIRKLARELI REVISION OF CATHODIC PROTECTION OF BOTAS MALKOCOGLU COMPRESSION STATION ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $16.000,00 2002 2003

81 ALPET MERSIN CATHODIC PROTECTION OF 8'' 1650M LAND AND 5000M SEA,12'' 1650M LAND AND 5000M SEA PIPE LINE

CATHODIC PROTECTION OF OIL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $43.000,00 2003 2003

82 ALPET KIRIKKALE CATHODIC PROTECTION OF FUEL STORAGE TANKS INTERNAL BOTTOM CATHODIC PROTECTION OF FUEL TANK BOTTOM+ENGINEERING+APPLICATION $67.000,00 2003 2003

84 ALPET KIRIKKALE-TUPRAS A CATHODIC PROTECTION OF FUEL PIPE LINE CATHODIC PROTECTION OF OIL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $58.000,00 2003 2003

85 ENERJI PETROL CATHODIC PROTECTON (WITH EXTERNAL CURRENT SOURCE) OF MERSIN FACILITIES 8" PETROLEUM PIPE LINE

CATHODIC PROTECTION OF OIL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $95.000,00 2003 FINISHED

86 GURIS ACK ORTAKLIGI CATHODIC PROTECTION OF Ø 2240 75 KM BUYUK MELEN DRINKING WATER PROJECT PIPE LINE

CATHODIC PROTECTION OF WATER PIPE LINE+ENGINEERING+SUPPLY OF MATERALS+APPLICATION $250.000,00 2003 FINISHED

87 ALSIM ALARKO RINGS ORTAKLIGI CATHODIC PROTECTION OF Ø 2240 75 KM DRINKING WATER PIPE LINE BUYUKMELEN PROJECT


88 ISKI-KALYON INSAAT CATHODIC PROTECTION OF Ø2200 7500M PIPE LINE BETWEEN CAMLICA AND SARAYBURNU


89 ISKI- TETAN INSAAT MAHMUTBEY M Ø1400 745 M, Ø1200 510M, Ø1000 1825M, Ø900 1154M, Ø800 2541M BORU HATTININ KAT.KOR.


90 DELTA PETROL CATHODIC PROTECTION OF FUEL STORAGE TANKS INTERNAL BOTTOM CATHODIC PROTECTION OF FUEL PIPE LINE+ENGINEERING+SUPPLY OF MATERIALS+APPLICATION $45.000,00 2003 FINISHED

91 YEDAS BASHRA -MANUFACTURING AND CATHODIC PROTECTION OF 1750M3 STEEL BIOGAS STORAGE TANK ENGINEERING+SUPPLY OF MATERIALS AND ASSEMBLY $47.800,00 2003 FINISHED

92 BTC-STA CATHODIC PROTECTION OF BAKU-TIBILIS CEYHAN PIPE LINE LOT B ENGINEERING+SUPPLY OF MATERIALS AND ASSEMBLY $600.000,00 2003 CONTINUING

93 BTC- PROJECT COORDINATION CATHODIC PROTECTION OF BAKU-TIBILIS CEYHAN TERMINAL ENGINEERING+SUPPLY OF MATERIALS AND ASSEMBLY $670.000,00 2004 CONTINUING

94 BSH- PROFILO CERKEZKOY CATHODIC PROTECTION OF UNDERGROUND GAS STORAGE TANKS ENGINEERING+SUPPLY OF MATERIALS AND ASSEMBLY $4.800,00 2003 2003

95 BOTAS-LIMAK CATHODIC PROTECTION OF 40" - 180 KM NATURAL GAS PIPE LINE BETWEEN GAZIANTEP -MERSIN

CATHODIC PROTECTION OF 190 KM PIPE LINE+ENGINEERING+APPLICATION ON THE FIELD+COMMISSIONING $200.000,00 2005 CONTINUING

96 BOTAS-ERKO CATHODIC PROTECTION OF HORASAN-PT1 NATURAL GAS PIPE LINE CATHODIC PROTECTION OF 210 KM PIPE LINE+ENGINEERING+APPLICATION ON THE FIELD+COMMISSIONING $210.000,00 2005 CONTINUING

97 TPAO-ADIYAMAN REGION CATHODIC PROTECTION OF ADIYAMAN DISTRICT OFFICE PIPE LINE PREPARING OF REHABILITATION PROJECT OF 145 KM PIPE LINE $12.500,00 2006 2006

99 ALPET CATHODIC PROTECTION (WITH EXTERNAL CURRENT SOURCE) OF MERSIN FACILITY 8'' PETROLEUM PIPE LINE ENGINEERING+SUPPLY OF MATERIALS AND ASSEMBLY $24.000,00 2007 CONTINUING


EN ISO 9001:2000



100 SCOP-AURAYSA KHURMALA DOME PROJECET-CATHODIC PROTECTION OF 2 UNITS OF 4700 M3 STORAGE TANKS ENGINEERING+SUPPLY OF MATERIALS $45.000,00 2007 CONTINUING

101SCOP-AURAYSA KHURMALA DOME PROJECT-CATHODIC PROTECTION OF NATURAL GAS AND

PETROLEUM PIPE LINEENGINEERING+SUPPLY OF MATERIALS

$198.000,00 2007CONTINUING

102BOTAS/METOT

CATHODIC PROTECTION OF SIVAS+HANAK+TURKOZUENGINEERING+SUPPLY OF MATERIALS AND ASSEMBLY

$65.000,00 2007CONTINUING





Page 45 of 146

EN ISO 9001:2000

SECTION -7

OOOUUURRR FFFLLLAAAOOOTTTIIINNNGGG SSSUUUCCCTTTIIIOOONNN PPPIIIPPPEEE AAANNNDDD RRREEEFFFEEERRREEENNNCCCEEESSS

Storageteck is a registered trademark of Ergil Group


Phone: +90 212 643 62 26 (Pbx) Fax: +90 212 643 62 22 Dubai Office:Rak Free Trade Zone P.O.Box:10559 Ras Al Khamiah U.A.E Factory:Atatürk Cad.OSB.Fatih Sitesi 6/a Blok Ikitelli-ISTANBUL/TURKEY


EN ISO 9001:2000

NO EMPLOYER PLACE DIAMETERS QUANTITY

1 MÖN İNŞAAT

SABİHA GÖKÇEN AIRPORT MANUFACTURE AND MOUNTING OF FLOATING SUCTION PIPE FOR JET A.1 FUEL TANKS AUTOMATIK SUCTION PIPE WITH 3- POINT SAMPLING SYSTEM

6” 3

2 MÖN İNŞAAT

SABİHA GÖKÇEN AIRPORT MANUFACTURE AND MOUNTING OF FLOATING SUCTION PIPE FOR JET A.1 FUEL TANKS AUTOMATIK SUCTION PIPE WITH 3- POINT SAMPLING SYSTEM

20” 3

3 ALTINBAŞ PETROL A.Ş

CYPRUS AIRLINES MANUFACTURE AND MOUNTING OF FLOATING SUCTION PIPE FOR CYPRUS AIRLINES JET A.1 FUEL TANKS DURING IN AIRPORT FUEL SERVICES FOR AIR

6” 4

4 ALTINBAŞ PETROL A.Ş

CYPRUS AIRLINES MANUFACTURE AND MOUNTING OF FLOATING SUCTION PIPE FOR CYPRUS AIRLINES JET A.1 FUEL TANKS IN ALTINBAS MAIN FILLING FACILITIES

8” 2

5 PETROL OFİSİ A.Ş ALİAĞA FILLING FACILITIES 3” 2

6 PETROL OFİSİ A.Ş ALİAĞA FILLING FACILITIES 8” 2





EN ISO 9001:2000

7 ÇEKİSAN HARAMİDERE FACILITIES 8” 2

8 SHELL COMPANY DERİNCE FACILITIES 8” 2

9 ÇEKİSAN İSKENDERUN FACILITIES 8” 2

10 ÇEKİSAN ANTALYA FACILITIES 8” 3




Page 47 of 146

EN ISO 9001:2000

Floating Suction Pipe




Page 48 of 146

EN ISO 9001:2000

SECTION -8

OOOUUURRR IIINNNTTTEEERRRNNNAAALLL FFFLLLOOOAAATTTIIINNNGGG RRROOOOOOFFF AAANNNDDD RRREEEFFFEEERRREEENNNCCCEEESSS




Page 49 of 146

EN ISO 9001:2000





NO EMPLOYER PLACE DIAMETERS

(meter) QUANTİTY RESPONSIBLE PHONE

ALİAĞA PLANT 14,32 2 CUMHUR KIZILENİŞ 0 232 625 12 50 10,50 2 CUMHUR KIZILENİŞ 0 232 625 12 50 1

EGE GÜBRE SANAYİİ A.Ş

9,95 3 CUMHUR KIZILENİŞ 0 232 625 12 50 30,5 1 GÜROL ACAR

SELAMİ TOPALOĞLU 0 216 522 9000

30,5 1 GÜROL ACAR SELAMİ TOPALOĞLU

0 216 522 9000

31,5 M 1 GÜROL ACAR SELAMİ TOPALOĞLU

0 216 522 9000

16.50 M 1 GÜROL ACAR SELAMİ TOPALOĞLU

0 216 522 9000


0 216 522 9000

ALİAĞA FILLING PLANT


0 216 522 9000


0 216 522 9000 MERSİN FILLING PLANT

21 M 4 GÜROL ACAR SELAMİ TOPALOĞLU

0 216 522 9000


0 216 522 9000

2 OPET PETROLCULUK

KÖRFEZ FILLING PLANT 13,17 M 1 GÜROL ACAR

SELAMİ TOPALOĞLU 0 216 522 9000

EN ISO 9001:2000

INTERNAL FLOATING ROOF REFERENCES Sayfa 2 / 2

NO EMPLOYER PLACE DIAMETERS (meter)

QUANTITY

RESPONSIBLE PHONE

3 SÖKTAŞ TEKSTİL FABRİKASI

AYDIN SÖKE FACTORY 300 M3 2 ADET

4 MENSA ADANA FACILITIES 300 M3 2 ADET

5 AKÇA ENERJİ DENİZLİ SARAYKÖY PLANT 300 M3 2 ADET

6 ÇEKİSAN DEPOLAMA

HARAMİDERE STORAGE FACILITIES

10 AND 11 NUMBER

TANK

2 ADET BORA ALTINAY 0 212 591 01 06

ALİAĞA PLANT NAPHTA TANK

∅ 78,5 M 0232 616 12 40

AROMATIC TANK

∅ 26,5 M 0232 616 12 40

ETHYLENE TANK

∅ 26 M 0232 616 12 40

7 PETKİM PETROKİMYA

ETHYLENE TANK ∅ 19 M 0232 616 12 40 ∅ 9,7 M 1 ADET ÖZGÜR ÖZCAN 0 324 239 03 10

8 YALIN PETROL MERSİN PLANT ∅ 11.4 M 1 ADET

9 TOTAL DİL WHARF PLANT ∅ 12,07 M 1 ADET NEVZAT BAYCAN 10 LİMAŞ DERINCE PLANT ∅ 17,00 M 3 ADET

EN ISO 9001:2000




Page 52 of 146

EN ISO 9001:2000

SECTION -9

OOOUUURRR TTTAAANNNKKK AAANNNDDD PPPIIIPPPIIINNNGGG RRREEEFFFEEERRREEENNNCCCEEESSS

ERGIL TANK AND PIPING REFERENCES-1 (Eng.); Date:30.09.2006 Sayfa 1 / 21 ERGIL GROUP INT www.ergilgroup.com, e-mail: [email protected]

EN ISO 9001:2000

( 1 ) ERGIL GROUP

TURN KEY PROJECTS REFERENCE LIST ABOUT STORAGE TANKS

(ENGINEERING-PROCUREMENT-FABRICATION- SITE INSTALLATION)


EN ISO 9001:2000

NO CLIENT PROJECT NAME AND THE LOCATION

KODIANA EMERGENCY DRAIN DOWN FACILITY IN GEORGIA

11

BBRRIITTIISSHH PPEETTRROOLLEEUUMM && BBTTCC CCoo.. ((EEPPCC)) TTAANNKK CCAAPPAACCIITTYY:: 88..550000 MM33

Manufacturing of underground tank includes a 8,500 m³ buried tank,designed with double containment. (8500m3 x 1 – according to API 650).

Engineering & Design Piping Valve mounting Manufacturing and mounting of concrete roof Projecting and Application of Cathodic Protection, Manufacture of Anodes Used

(Tank Inner Bottom and Underground pipes) Mounting of Pumps Mounting of Tank Accessories

a. Flame Arresters b. Pressure Vacuum Vents c. Gauge Hatches d. Non-atmospheric Gauge Hatch

1. Manufacture and Mounting of Fire Protection Foam Expulsion Systems 2. Manufacture and Mounting of Tank Cooling Spring System 3. Complete Construction Work

a. Foundations b. Peripheral Protection Walls c. Switch Board – Control Room d. Manufacture of Pipe Ducts e. Stabilization, Leveling and Preparation of the site d. Telecommunication

Supply, Manufacture and Mounting of Materials Testing of Entire System (Hydraulic tests + Radiography of welding places) Start-up

START DATE JUNE 2006 DATE OF COMPLETION CONTINUE LABOUR FORCE

(DAY X WORKER) 250.000


EN ISO 9001:2000

NO CLIENT PROJECT NAME AND SCOPE

MERSIN ADANALIOGLU LOADING TERMINAL

22

EENNEERRJJII PPEETTRROOLL AA..SS // MMEERRSSIINN // TTUURRKKEEYY

((EEPPCC))

TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 1199 335500 MM33

Manufacturing of tanks (API 650) 4 X 5000 m3 8 X 1000 m3 3 X 450 m3 2” 3.500 mt 12” 28 mt 4” 750 mt 6” 1250 mt 8” 750 mt

Assembling of vents Manufacturing and assembling of internal Floating roof Preparing the Project for Cathodic Protection-Application –Manufacturing of anodes (Inner Tank Base and Underground

Pipes) Painting of of inside and outside of Tanks Fuel Pipe Line Assembling of pumpsı Construction of 2 units of collectors Construction of 2 units of vent roomı Construction of triple filling blocks Manufacturing and Assembling of Tank Accessories Flame Arrestors Pressure Vacuum Vents Gage Hatches Gaeg Hatches close to the atmosphere Manufacturing and Assembling of Fire Extinguishing-Foam Launching systems Manufacturing and Assembling of Tank Cooling Systems and Spring systems Composing preliminary Purification System Construction of Steel balustrades Supplying,manufacturing and assembling of materials Complete construction work Bases Complete Environmental protection walls, Steel balustrades and doors

-Control panel-Control room -Stabilisation of the field -Manufacturing of pipes

Test of complete system (%100 non-destructive testing and hydrostatic pressure tests) Putting the system into service

START DATE SEPTEMBER

2003 DATE OF

COMPLETION 2005

LABOUR FORCE (Worker x Day)


EN ISO 9001:2000


KIRIKKALE STORAGE TANK CONSTRUCTION

33

AALLTTIINNBBAASS PPEETTRROOLL AA..SS AALLPPEETT ((EEPPCC))

TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY::

3366..550000 mm33

Manufacturing of tanks (API 650) 5 x 5.000 m3 10 x 1.000 m3 3 x 500 m3

Painting of of inside and outside of Tanks Fuel Pipe Line Assembling of Vents Preparing the Project for Cathodic Protection-Application –Manufacturing of anodes (Inner Tank Base and Underground

Pipes a. Assembling of pumpsı b. Construction of 2 units of collectors c. Construction of 2 units of vent roomı d. Construction of triple filling blocks

Manufacturing and Assembling of Tank Accessories a. Flame Arrestors b. Pressure Vacuum Vents c. Gage Hatches d. Gaeg Hatches close to the atmosphere

Manufacturing and Assembling of Fire Extinguishing-Foam Launching systems Manufacturing and Assembling of Tank Cooling Systems and Spring systems Composing preliminary Purification System Construction of Steel balustrades Supplying and assembling of materials Test of complete system (%100 non-destructive testing and hydrostatic pressure tests) Putting the system into service

START DATE JUNE 2003 DATE OF

COMPLETION NOVEMBER 2004

LABOUR FORCE (Worker x Day)

3000


EN ISO 9001:2000

NO CLIENT PROJECT NAME AND THE LOCATION IZMIT FILLING FACILITIES

44

AALLTTIINNBBAASS PPEETTRROOLL AA..SS IIZZMMIITT DDOOLLUUMM TTEESSIISSLLEERRII ((EEPPCC)) TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 2299..335500 MM33

Manufacture of tanks (according to API 650) ♦ 2 X 5000 m3 ♦ 8 X 1000 m3 ♦ 3 X 450 m3

Dying of Tank’s Inner and Outer Shell Fuel Pipeline

2” 3.500 m. 4” 750 m. 6” 1250 m. 8” 70 m. 12” 28 m.

Valve mounting Manufacture and mounting of internal floating ceiling Projecting and Application of Cathodic Protection, Manufacture of Anodes Used (Tank Inner Bottom and

Underground pipes) Mounting of Pumps Construction of 2 collectors Building of 2 Vents Rooms Building of triple filling room Manufacture and Mounting of Canopy Manufacture and Mounting of Tank Accessories

Flame Arresters Pressure Vacuum Vents Gauge Hatches Non-atmospheric Gauge Hatch

Manufacture and Mounting of Fire Protection Foam Expulsion Systems Manufacture and Mounting of Tank Cooling Spring System Establishing of pre-refining system Peripheral guard fence (steel construction) Supply, Manufacture and Mounting of Materials Testing of the Entire System (Inspections without 100% destruction and Hydrostatic pressure tests) Start-up

START DATE 2000 DATE OF

COMPLETION 2001

LABOR FORCE (Worker x Day)

2200


EN ISO 9001:2000

NO CLIENT PROJECT NAME AND THE LOCATION OPET MERSIN TERMINAL

55

OOPPEETT –– MMEERRSSIINN ((EEPPCC)) TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 1155..000000 mm33

Manufacture of tanks (according to API 650) ♦ 15.000 m3


2” 500 m. 4” 450 m. 6” 250 m. 8” 170 m. 12” 2850 m.

Valve mounting Manufacture and mounting of internal floating ceiling Projecting and Application of Cathodic Protection, Manufacture of Anodes Used (Tank Inner Bottom and

Underground pipes) Mounting of Pumps Construction of 2 collectors Building of 2 Vents Rooms Building of triple filling room Manufacture and Mounting of Canopy Manufacture and Mounting of Tank Accessories


Manufacture and Mounting of Fire Protection Foam Expulsion Systems Manufacture and Mounting of Tank Cooling Spring System Establishing of pre-refining system Peripheral guard fence (steel construction) Supply, Manufacture and Mounting of Materials Testing of the Entire System (Inspections without 100% destruction and Hydrostatic pressure tests) Start-up


COMPLETION 2003


2000


EN ISO 9001:2000

SIRA NO CLIENT PROJECT NAME AND LOCATION

MERSIN, TURN-KEY PETROLEUM STORAGE TERMINAL

66

AALLTTIINNBBAASS PPEETTRROOLL AA..SS.. MMEERRSSIINN OOIILL SSTTOORRAAGGEE TTEERRMMIINNAALL ((EEPPCC)) TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 2233..990000 MM33

Manufacture of tanks (according to API 650) 3 X 5000 m3 8 X 1000 m3 2 X 300 m3


2” 3500 m 12” 400 m 4” 2880 m 16” 75 m 6” 3250 m 24” 60 m 8” 6000 m

Valve mounting Manufacture and mounting of internal floating ceiling Projecting and Application of Cathodic Protection, Manufacture of Anodes Used (Tank Inner Bottom and Underground pipes) Mounting of Pumps Construction of 2 collectors Building of 2 Vents Room Building of triple filling room Manufacture and Mounting of Canopy Manufacture and Mounting of Tank Accessories


Manufacture and Mounting of Fire Protection Foam Expulsion Systems Manufacture and Mounting of Tank Cooling Spring System Establishing of pre-refining system Peripheral guard fence (steel construction) Supply, Manufacture and Mounting of Materials Complete Construction Work Foundations Peripheral Protection Walls + Steel guard fence and doors Switch Board – Control Room Manufacture of Pipe Ducts Stabilization of the site Testing of the Entire System (Inspections without 100% destruction and Hydrostatic pressure tests) Start-up


COMPLETION 2002


2200


EN ISO 9001:2000


MERSIN, OIL STORAGE TERMINAL II. Phase

77

AALLTTIINNBBAASS PPEETTRROOLL AA..SS.. MMEERRSSIINN OOIILL SSTTOORRAAGGEE TTEERRMMIINNAALL ((EEPPCC)) TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 3300..110000 MM33

Manufacture of tanks (according to API 650) 4 X 5000 m3 3 X 2500 m3 2 X 1000 m3 2 X 300 m3


2” 3500 m 12” 400 m 4” 2880 m 16” 75 m 6” 3250 m 24” 60 m





COMPLETION 2005



EN ISO 9001:2000


KIRKLARELI TANK FIELD CONSTRUCTION

88

EENNEERRJJII PPEETTRROOLL AASS.. ((EEPPCC)) TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 44..772200 MM33

Manufacture of tanks (according to API 650) 4 X 1000 m3 2 X 300 m3 2 X 60 m3


4” 2880 m 16” 75 m 6” 3250 m 24” 60 m 8” 900 m





COMPLETION 2005



EN ISO 9001:2000


NNOORRTTHH CCYYPPRRUUSS TURN-KEY PETROLEUM STORAGE TERMINAL

99

AALLTTIINNBBAASS PPEETTRROOLL AA..SS.. NNOORRTTHH CCYYPPRRUUSS OOIILL SSTTOORRAAGGEE TTEERRMMIINNAALL ((EEPPCC)) TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 22..000000 MM33

Manufacture of tanks (according to API 650)

Tank Capacity: 2 X 1000 m3 Dying of Tank’s Inner and Outer Shell Fuel Pipeline

8” 400 m 4” 1500 m 6” 1250 m





COMPLETION 2002



EN ISO 9001:2000

NO CLIENT PROJECT NAME AND SCOPE MANUFACTURING OF A TANK OF CAPACITY 1000 M3

1100

PPOOAAŞŞ -- IIZZMMIITT LLUUBBEE OOIILL FFAACCIILLIITTIIEESS

((EEPPCC))

TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 11000000 mm33

Manufacturing of tanks (API 650) Tank Capacity : 1 X 1000 m3

Assembling of Valves Preparing a Project for Cathodic Protection-Application–Manufacturing of Anodes Assembling of pumps Manufacturing and Assembling of Tank Accessories

a. Flame Arrestors b. Pressure Vacuum Vents c. Gage Hatches d. Gage Hatches Closed to atmosphere

Manufacturing,obtaining and assembling of materials Full construction work Bases

a. Environmental protection walls-Steel balustrades and doors b. Control panel-Control room c. Stabilisation of the field

Test of complete system (%100 non-destructive testing and hydrostatic pressure tests) Putting

the system into service

START DATE JANUARY 2003 DATE OF

COMPLETION MARCH 2003



EN ISO 9001:2000


NAPHTA STORAGE FACILITY AND MECHANICAL WORKS

1111

AAYYDDIINN SSOOKKEE SSÖÖKKTTAAŞŞ TTEEXXTTIILLEE FFAACCTTOORRYY

FFAACCIILLIITTYY ((EEPPCC))


660000 mm33

Manufacture of tanks (according to API 650) Tank Capacity: 2 x 300 m3

Dying of Tank’s Inner and Outer Shell Piping Valve mounting Manufacture and mounting of internal floating ceiling Projecting and Application of Cathodic Protection Manufacture of Anodes Used (Tank

Inner Bottom and Underground pipes) Mounting of Pumps Manufacture and Mounting of Tank Accessories

• Flame Arrester • Pressure Vacuum Vents • Gauge Hatches • Non-atmospheric Gauge Hatch

Manufacture and Mounting of Fire Protection Foam Expulsion Systems Manufacture and Mounting of Tank Cooling Spring System Complete Construction Work

♦ Foundations ♦ Peripheral Protection Walls ♦ Switch Board – Control Room ♦ Manufacture of Pipe Ducts ♦ Stabilization, Leveling and Preparation of the site

Supply, Manufacture and Mounting of Materials Testing of Entire System (Hydraulic tests + Welding röntgen films) Start-up


2001 DATE OF

COMPLETION 2002


1600


EN ISO 9001:2000



1122 AADDAANNAA MMEENNSSAA

FFAACCIILLIITTIIEESS

Manufacture of tanks according to API 650 Tank Capacity : 2 x 300 m3

Dying of Tank’s Inner and Outer Shell Piping Valve mounting Manufacture and mounting of internal floating ceiling Projecting and Application of Cathodic Protection, Manufacture of Anodes Used

(Tank Inner Bottom and Underground pipes) Mounting of Pumps Manufacture and Mounting of Tank Accessories



Foundations Peripheral Protection Walls Switch Board – Control Room Manufacture of Pipe Ducts Stabilization, Leveling and Preparation of the site

Supply, Manufacture and Mounting of Materials Testing of the Entire System (Hydraulic tests + Radiography of Welding) Start-up

START DATE MAY 2000 DATE OF

COMPLETION JULY 2000


1600


EN ISO 9001:2000



1133

AAKKCCAA EENNEERRJJII SSAARRAAYYKKOOYY FFAACCIILLIITTIIEESS ((EEPPCC)) TTAANNKK CCAAPPAACCIITTYY:: 660000 MM33

Manufacture of tanks according to API 650 Tank Capacity: 2 x 300 m3

Dying of Tank’s Inner and Outer Shell Piping Valve mounting Manufacture and mounting of internal floating ceiling Projecting and Application of Cathodic Protection, Manufacture of Anodes Used

(Tank Inner Bottom and Underground pipes) Mounting of Pumps Manufacture and Mounting of Tank Accessories

a. Flame Arresters b. Pressure Vacuum Vents c. Gauge Hatches d. Non-atmospheric Gauge Hatch


a. Foundations b. Peripheral Protection Walls c. Switch Board – Control Room d. Manufacture of Pipe Ducts e. Stabilization, Leveling and Preparation of the site

Supply, Manufacture and Mounting of Materials Testing of Entire System (Hydraulic tests + Radiography of Welding) Start-up


2001 DATE OF

COMPLETION 2002


1600


EN ISO 9001:2000

( 2 ) ERGIL GROUP REFERENCE LIST

ABOUT STORAGE TANKS AS ENGINEERING-PROCUREMENT-FABRICATION


EN ISO 9001:2000

NO CLIENT PROJECT NAME AND THE LOCATION BASRAH, IRAQ INTERNATIONAL AIRPORT STORAGE TANK FACILITY

11

KKeelllloogg BBrroowwnn && RRoooott // HHaalllliibbuurrttoonn,, UU..SS..AA

((EEPP))

TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 1100..000000 MM33

Prefabrication of tanks 5000M3 Aluminium Dome Roof Storage Tank & 5000m3 External Floating Roof Gasoline Tank According to API 650

Engineering & Design Manufacture and mounting of internal floating ceiling Projecting and Manufacturing of Cathodic Protection Materials Mounting of Pumps Manufacture of Tank Accessories

• Flame Arrester • Pressure Vacuum Vents • Gauge Hatches • Non-atmospheric Gauge Hatch ...etc

Manufacture of Fire Protection Foam Expulsion Systems Manufacture and Mounting of Tank Cooling Spring System Supply, Manufacture of Complete S.T Materials Supply and Procurement of Complete Manufacturing Equipment & Materials

START DATE January 2006

DATE OF COMPLETION

July 2006



EN ISO 9001:2000


KHURMALA DOME DEVELOPMENT PROJECT FLOW TANKS

22

AAVVRRAASSYYAA TTEECCHHNNOOLLOOGGYY AA..SS.. ((EEPP))


99..335500 MM33

Crude Oil Storage Tank– according to API 650 Tank Capacities :

2 x 4767 m3 Enginneering & Design of Tanks according to API 650 Blasting and Painting of Tank’s Inner and Outer Shell Projecting and Manufacture of Cathodic Protection Materials Mounting of Pumps Manufacture of Tank Accessories

Flame Arresters Pressure Vacuum Vents Gauge Hatches Non-atmospheric Gauge Hatch ...etc

Manufacture of Fire Protection Foam Expulsion Systems Manufacture of Tank Cooling Spring System Supply, Manufacture and Mounting of Materials

START DATE JUNE 2006 DATE OF

COMPLETION CONTINUE



EN ISO 9001:2000

NO CLIENT PROJECT NAME AND SCOPE CONSTRUCTION of BIOGAS STORAGE TANK IN BASHRA

33

YYEEDDAASS AA..SS BBAASSRRAA // IIRRAAQQ

((EEPP))

TTOOTTAALL TTAANNKK CCAAPPAACCIITTYY:: 33..550000 mm33

Tank Capacity: 2X1750 M3 Preparing Project of Tank Preparing Project reinforced concrete pool Preparing the Project for Cathodic Protection Supply of Material

Supply of complete steel plates Supply of RMS station Supply of Tank Accessories Supply of Cathodic protection materials

Assembling a. Bending and assembling of plates b. Construction of reinforced concrete pool c. Assembling of Cathodic Protection System

Assembling a. Complete %100 non-destructive testing b. Hydrostatic Tests

Stabilisation of the field Putting the system into service

START DATE JANUARY 2003 DATE OF

COMPLETION CONTINUING



EN ISO 9001:2000

( 3 ) ERGIL GROUP REFERENCE LIST

ABOUT STORAGE TANKS AS MAINTENANCE and REPAIR WORK of TANK


EN ISO 9001:2000


MAINTENANCE and REPAIR WORK of TANK FIELD

11 DDEELLTTAA PPEETTRROOLL AA..SS DDOORRTTYYOOLL TTEERRMMIINNAALL // TTUURRKKEEYY

Tank -34 (5.000 m3)

• Blasting of internal and external plates, • Painting, • Renovation of Tank base concrete, • Renovation of internal antigorite pipes, • Renovation of pipe connections • Renovation and maintenance of base concrete

Tank -21 (3.000 m3)

• Blasting of internal and external plates, • Painting, • Renovation of Tank base concrete, • Renovation of internal antigorite pipes, • Renovation of pipe connections • Renovation and maintenance of base concrete

Boiler Room

• Maintenance and repairing, • Changing of Boiler rooms completely


2003 DATE OF

COMPLETION 2006



EN ISO 9001:2000


12 RENOVATION OF FLOATING ROOF STORAGE TANKS AND CONSTRUCTION OF FIRE PROTECTION SYSTEMS

22 PPEETTKKIIMM AA..SS // IIZZMMIIRR

Tank Capacity 12 x 20.000 m3

Disassembling of seal systems

Assembling of new seal systems

Assembling of over tank alarm systems

Laying 20.000 meters of cable (undergroundı-over ceiling-inside channel)

Assembling of control panels in 5 units of secondary and in main building

START DATE NOVEMBER 2001 DATE OF

COMPLETION MARCH 2002


950




Page 85 of 146

EN ISO 9001:2000

SECTION -10

PPPRRREEESSSSSSUUURRREEE VVVEEESSSSSSEEELLL




Page 87 of 146

EN ISO 9001:2000

ORDER NUMBER

1

EMPLOYER;

NAME of THE PROJECT; BOTAS DOGUBAYAZIT COMPRESSOR STATION BLOW DOWN

SILENCERS and FLAME ARRESTORS

DDOOGGUU BBAAYYAAZZIITT CCOOMMPPRREESSSSOORR SSTTAATTIIOONN BBLLOOWW DDOOWWNN SSIILLEENNCCEERR AAnndd FFLLAAMMEE AARRRREESSTTOORRSS <<9900 ddBB

66”” SSIILLEENNCCEERR aanndd FFLLAAMMEE AARRRREESSTTOORR

<<9900 ddBB

BBLLOOWW DDOOWWNN SSIILLEENNCCEERR AAnndd FFLLAAMMEE AARRRREESSTTOORRSS

<<9900 ddBB




Page 88 of 146

EN ISO 9001:2000

ORDER

NUMBER 2

EMPLOYER;

NAME of THE PROJECT;

BOTAS DOGUBAYAZIT COMPRESSOR STATION, BLOW DOWN SILENCERS and FLAME ARRESTORS

BBLLOOWW DDOOWWNN SSIILLEENNCCEERR AAnndd FFLLAAMMEE AARRRREESSTTOORRSS <<9900 ddBB

BBLLOOWW DDOOWWNN SSIILLEENNCCEERR AAnndd FFLLAAMMEE AARRRREESSTTOORRSS <<9900 ddBB

66”” SSIILLEENNCCEERR aanndd FFLLAAMMEE AARRRREESSTTOORR

<<9900 ddBB

BBLLOOWW DDOOWWNN SSIILLEENNCCEERR AAnndd FFLLAAMMEE AARRRREESSTTOORRSS

<<9900 ddBB

RELEVANT PERSON TELEPHONE NUMBER




Page 89 of 146

EN ISO 9001:2000

ORDER

NO; 3

EMPLOYER;

NAME of THE PROJECT; PETKIM CHIMNEY FIRE HEADERS ( MATERIAL; HASTELLOT B-2 )

PPEETTKKIIMM CCHHIIMMNNEEYY HHEEAADDEERR ((MMAATTEERRIIAALL ;; HHAASSTTEELLLLOOYY BB--22 ))

PPEETTKKIIMM CCHHIIMMNNEEYY HHEEAADDEERR ((MMAATTEERRIIAALL;; HHAASSTTEELLLLOOYY BB--22 ))

PPEETTKKIIMM CCHHIIMMNNEEYY HHEEAADDEERR ((MMAATTEERRIIAALL;; HHAASSTTEELLLLOOYY BB--22 ))

PRODUCT NAME

PIG RECEIVER AND

LAUNCHER




Page 90 of 146

EN ISO 9001:2000

CUSTOMER OPET PETROLEUM CO.-TURKEY

SIZE 24”X28” QUANTITY 4 PRODUCT YEAR

1997

DESIGN PRESSURE

70 Barg

DESIGN TEMPERATURE

-20/+70 oC

TEST PRESSURE

105

MATERIALS ASTM A 572 GR 50

FUNCTION MERSİN OPET TESİSLERİNDE BORU HATTINA PİG ATMAK VE

ALMAK AMACIYLA KULLANILMIŞTIR.

STANDART ASME SECTION VIII Div.1

PRODUCT NAME PIG RECEIVER AND

LAUNCHER




Page 91 of 146

EN ISO 9001:2000

CUSTOMER SANAYE PARTO NASB-IRAN

SIZE 30”X36” QUANTITY 2 PRODUCT YEAR 2005 DESIGN PRESSURE 30 Barg DESIGN TEMPERATURE

-20/+70 oC

TEST PRESSURE 48 MATERIALS API X42

FUNCTION DOĞAL GAZ BORU HATTINA PİG ATMAK VE ALMAK AMACIYLA

KULLANILMIŞTIR. STANDART ASME SECTION VIII

Div.1




Page 92 of 146

EN ISO 9001:2000

OTHER PRESSURE VESSEL

No CLIENT LOCATION SIZE QUANTITYSANDART PRESSURE

CLASS 1 LİMAŞ DEPOLAMA İZMİT STORAGE TERMINAL 8" 10 ASME SECTION VIII Div.1 300 Class 2 POAŞ MERSİN STORAGE TERMINAL 24" 2 ASME SECTION VIII Div.1 300 Class 3 ALTINBAŞ PETROL A.Ş İZMİT STORAGE TERMINAL 12" 4 ASME SECTION VIII Div.1 300 Class 4 ALTINBAŞ PETROL A.Ş KIBRIS STORAGE TERMINAL 8" 2 ASME SECTION VIII Div.1 300 Class 5 PETROL OFİSİ A.Ş ALİAĞA STORAGE TERMINAL 8" 2 ASME SECTION VIII Div.1 300 Class 6 SHELL COMPANY DERİNCE PETROLEUM STORAGE TERMINAL 8" 2 ASME SECTION VIII Div.1 300 Class 7 ÇEKİSAN HARAMİDERE STORAGE TERMINAL 8" 2 ASME SECTION VIII Div.1 300 Class 8 HAVATEK POAŞ ANTALYA STORAGE TERMINAL 12" 2 ASME SECTION VIII Div.1 300 Class 9 OPET PETROLCÜLÜK MERSİN STORAGE TERMINAL 28" 3 ASME SECTION VIII Div.1 300 Class

10 ÇORUM OSB ÇORUM OSB NATURAL GAS PIPELINE 8" 2 ASME SECTION VIII Div.1 600 Class 11 DELTA PETROL GÜRCİSTAN TANK STORAGE FARM AND PETROELUM PIPELINE 20" 2 ASME SECTION VIII Div.1 150 Class 12 ÇOLAKOĞLU -BOTAŞ KONYA 40" NATURAL GAS PIPELINE 40"X48" 2 ASME SECTION VIII Div.1 600 Class 13 ÇAĞDAŞ -BOTAŞ ESKİŞEHİR -8" NATURAL GAS PIPELINE 8"X12" 2 ASME SECTION VIII Div.1 600 Class 14 ALTINBAŞ PETROL A.Ş İZMİR MARINE PIPELINE 12X16" 2 ASME SECTION VIII Div.1 300 Class 15 ALTINBAŞ PETROL A.Ş İZMİR MARINE PIPELINE 16X20" 2 ASME SECTION VIII Div.1 300 Class 16 ALTINBAŞ PETROL A.Ş İZMİR MARINE PIPELINE 20X24 2 ASME SECTION VIII Div.1 300 Class 17 SANAYE PARTO NASB /IRAN ESFAHAN-İRAN 30"36" 2 ASME SECTION VIII Div.1 300 Class




Page 93 of 146

EN ISO 9001:2000

SECTION –11

PPPIIIGGG RRREEECCCEEEIIIVVVEEERRR /// LLLAAAUUUNNNCCCHHHEEERRR AAANNNDDD PPPIIIPPPIIINNNGGG RRREEEFFFEEERRREEENNNCCCEEESSS

<

PIG RECEIVER & LAUNCHER REFERENCES

No END USER EPC CO. / TRADE CO.SIZE

(BarrelxNeck) Qty. CLASSPIPELINE (DiaxThick.)

APPLICABLE Code/Std PROJECT NAME YEAR STATUS

1 LIMAS DEPOLAMA A.S. 8" 10 300 Cl 12 Asme Sec.VIII Div.I 2001 Completed2 PETROL OFISI A.S. PETROL OFISI A.S. / TURKEY 24" 2 300 Cl 16 Asme Sec.VIII Div.I 2001 Completed3 ALTINBAS PETROL A.S. ALTINBAS PETROL A.S. / TURKEY 12" 4 300 Cl 12 Asme Sec.VIII Div.I Mersin Terminal 2001 Completed4 ALTINBAS PETROL A.S. ALTINBAS PETROL A.S. / TURKEY 8" 2 300 Cl 12 Asme Sec.VIII Div.I Aliaga Terminal 2004 Completed5 PETROL OFISI A.S. PETROL OFISI A.S. / TURKEY 8" 2 300 Cl 12 Asme Sec.VIII Div.I 2005 Completed6 HAVATEK HAVATEK / TURKEY 12" 2 300 Cl 12 Asme Sec.VIII Div.I 2004 Completed7 OPET PETROLCULUK OPET PETROLCULUK / TURKEY 28" 3 300 Cl 18 Asme Sec.VIII Div.I 2003 Completed8 CORUM OSB 8" 2 600 Cl 12 Asme Sec.VIII Div.I Marmara Terminal 2004 Completed9 DELTA PETROL A.S. DELTA PETROL A.S. / TURKEY 20" 2 150 Cl 16 Asme Sec.VIII Div.I 2005 Completed10 BOTAS COLAKOGLU / TURKEY 48"x40 2 600 Cl 24 Asme Sec.VIII Div.I 2005 Completed11 BOTAS CAGDAS / TURKEY 12"x8" 2 600 Cl 16 Asme Sec.VIII Div.I 2005 Completed12 ALTINBAS PETROL A.S. ALTINBAS PETROL A.S. / TURKEY 16"x12" 2 300 Cl 18 Asme Sec.VIII Div.I 2006 Completed13 ALTINBAS PETROL A.S. ALTINBAS PETROL A.S. / TURKEY 20"x16" 2 300 Cl 18 Asme Sec.VIII Div.I 2006 Completed14 ALTINBAS PETROL A.S. ALTINBAS PETROL A.S. / TURKEY 24"x20" 2 300 Cl 18 Asme Sec.VIII Div.I 2006 Completed15 NATIONAL OIL CO. / IRAN SANAYE PORTO NASB / IRAN 36"x30 2 300 Cl 22 Asme Sec.VIII Div.I 2006 Completed16 OPET PETROLCULUK OPET PETROLCULUK / TURKEY 20"x16" 2 300 Cl 18 Asme Sec.VIII Div.I 2006 Completed17 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 20"x16" 1 300 Cl 14 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed18 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 18"x16" 1 300 Cl 14 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed19 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 22"x20" 3 300 Cl 16 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed20 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 24"x20" 3 300 Cl 16 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed21 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 26"x24 2 150 Cl 18 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed22 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 28"x24" 2 150 Cl 18 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed23 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 6"x4" 1 300 Cl 8,56 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed24 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 8"x6" 1 300 Cl 10 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed25 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 10"x8" 1 300 Cl 12 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed26 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 8"x4 1 300 Cl 8,56 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed27 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 10"x6" 1 300 Cl 10 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed28 SCOP / IRAQ KAR AVRASYA OILGAS SERVICE CO./ IRAQ 12"x8" 1 300 Cl 12 Asme Sec.VIII Div.I Khurmala Dome 2006 Completed29 OPET PETROLCULUK OPET PETROLCULUK / TURKEY 32"x36" 2 150 Cl 32 Asme Sec.VIII Div.I Marmara Project 2007 Continue 30 OPET PETROLCULUK OPET PETROLCULUK / TURKEY 36"x40 2 150 Cl 36 Asme Sec.VIII Div.I Marmara Project 2007 Continue 31 TOTAL / SYRIA AL EMAD TRADING CO. / UAE 12"x16 2 150 Cl 12 Asme Sec.VIII Div.I Jafra-Qahar Pipe Line Project 2007 Continue




Page 94 of 146

EN ISO 9001:2000

PPİİGG RREECCEEIIVVEERR//LLAAUUNNCCHHEERR




Page 96 of 146

EN ISO 9001:2000

SECTION -12

TTTAAANNNKKK AAACCCCCCEEESSSSSSOOORRRIIIEEESSS




Page 97 of 146

EN ISO 9001:2000

PRESSURE VACUUM VENT

In atmospheric storage tanks with stable roof, where petroleum products

are stored

In expulsing of the excess oxygen to atmosphere, which appears

during good entry to tank, in the most cost-efficient way

To eliminate happening of vacuum while discharging of tank

In allowing the air to penetrate tank from atmosphere

In getting rid of vacuum and pressure that caused by temperature

difference between day and night, and air temperature variation,

without corrupting tank safety

Various breathers with flame arrester of different sizes and quantity

depending on tank size, and maximum number of goods in and out of

tank are used

These vents, minimize tank shrinkage, and reduce economically air

pollution, are useful for atmospheric ecological equilibrium

Technical Specifications They are generally manufactured in sizes of 2”, 3”, 4”, 6”, 8”, 10”, 12”

Manufacturing Materials: Aluminum, which is not effected by petroleum products and their steam, AISI 316 stainless steel, asbestos teflon gaskets, and rust resisting bolts.




Page 98 of 146

EN ISO 9001:2000

Body Material Body Material is rust resisting aluminum cast that do not spark due to friction and

beat, and is resistant against petroleum products steam.

Other materials may be used in the event of special orders. The flat may be coated

with aluminum plate, also manufactured as aluminum cast. Materials of this process

have ex-proof, and spark proof specifications.

PRESSURE-VACUUM VENT (BREATHER)SIZE 2" 3" 4" 6" 8" 10" 12"A 52 78 100 150 200 255 304B 120 152,2 170 225 280 362 432C 270 370 480 568 668 915 1060D 205 260 375 375 375 670 670

Clacks Clacks are sections, where breathing occurs and which are likely to be destructed by

petroleum steam, their bearing spindles are AISI 316 stainless steel, and their eloxal

aluminum surfaces are coated with asbestos teflon. The surface, on which claks are

placed, is reinforced with teflon oringle, and fit on each other. In this way, undesired

leakages are minimized between two interfaces.

The help of the lead masses placed on clacks can obtain desired pressure and

vacuum values. No spring is utilized for such process.

Bearing in Clacks: Caterpillar of clacks is loosely guided around, and on center. Spring is not used.

Since guiding is loose and free, possible compression and non-operation do not

occur




Page 99 of 146

EN ISO 9001:2000

Connecting Flanges to Tank:

Connecting section’s design is mounted to flanges compatible with ASA Class 150.

They may be used in other norms on request.

Device Sections:

1) Pressure Clack Section

2) Vacuum Clack Section

All materials, used in Pressure vacuum vent, have characteristic of not expulsing

spark due to beats. They are resistant to corrosion petroleum product steam.

The main body is a sturdy aluminum cost. O` ringlers of vacuum section have been

mounted to this body in a way to allow to remove, and change when necessary. Its

vent clacks, which are eloxal aluminum, loosely guided around and on center, have

been mounted without causing any compression. Peripheral, and central bearing

spindles are made with AISI 316 stainless steel.

Clacks surfaces are plated with asbestos teflon gasket. The surface, which clack will

push, is shaped as a knife blade, and teflon has been slipped on the blade. Matching

of one to another has been totally ensured, and undesired leakages have been

minimized.

Pressure, vacuum, and capacity values are given in the graphics. The device is to

be delivered after adjustment to desired values. The tag on it subsequently shows

vacuum and capacity in “m3/hour”. The section under the vacuum clack is designed

not to let remnants to accumulate, which are caused by condensation of petroleum

steam. Drilling in other norms is available on request.




Page 100 of 146

EN ISO 9001:2000

Maintenance:

Valves should be cleaned within definitive periods of time according to weather,

enterprise conditions, and especially the surface, on which vacuum clacks contact

should be extremely clean. Valves should be all removed, and cleaned. Their guide

shafts should slightly be oiled. The oil should be resistant to petroleum steam.

Pressure and vacuum clacks may be taken out, maintained, and cleaned after easy

opening of upper cover.

Pressure Safety Vent Pressure Safety Vent (Breathers)

In atmospheric storage tanks with stable roof, where petroleum products are stored;

Pressure Safety Vents are useful in expulsing of the excess oxygen to atmosphere, which appears during good entry to tank, in the most cost-efficient way.

Since these vents minimize tank shrinkage and reduce economically air pollution

Technical Specifications

They are generally manufactured in sizes of 2”, 3”, 4”, 6”, 8”, 10”, 12”

Manufacturing Materials:

Aluminum, which is not effected by petroleum products and their steam, AISI 316

stainless steel, asbestos teflon gaskets, and rust resisting bolts.

Body Material:

Body Material is rust resisting aluminum cast that do not spark due to friction and


Other materials may be used in the event of special orders. The flat may be coated

with aluminum plate, also manufactured as aluminum cast.




Page 101 of 146

EN ISO 9001:2000

Clacks surfaces are plated with asbestos teflon gasket. The surface, which clack will

push, is shaped as a knife blade, and teflon has been slipped on the blade. Matching

of one to another has been totally ensured, and undesired leakages have been

minimized.

By the help of the lead masses placed on clacks can obtain desired pressure and


Connecting holes have been drilled in compliance with flanges sizes in ASA Class

150.

None of the cross sections surface is lower than devices said diameters.

Pressure, vacuum, and capacity values are given in the graphics. The device is to

be delivered after adjustment to desired values. The tag on it subsequently shows

vacuum and capacity in “m3/hour”. The section under the vacuum clack is designed

not to let remnants to accumulate, which are caused by condensation of petroleum

steam. Drilling in other norms is available on request.

Maintenance:

Valves should be cleaned within definitive periods of time according to weather,

enterprise conditions, and especially the surface, on which vacuum clacks contact

should be extremely clean. Valves should be all removed, and cleaned. Their guide

shafts should slightly be oiled. The oil should be resistant to petroleum steam. Flame

arrester honeycombs should be cleaned with pressure air from time to time.

Pressure and vacuum clacks may be taken out, maintained, and cleaned after easy

opening of upper cover.




Page 102 of 146

EN ISO 9001:2000

Clacks:

Clacks are sections, where breathing occurs and which are likely to be destructed by







Bearing in Clacks:

Caterpillar of clacks is loosely guided around, and on center. Spring is not used.


occur.

Device Sections:

All materials, used in Pressure vacuum vent, have characteristic of not expulsing

spark due to beats. They are resistant to corrosion petroleum product steam.

The main body is a sturdy aluminum cost. O` ringlers of vacuum section have been

mounted to this body in a way to allow to remove, and change when necessary. Its

vent clacks, which are eloxal aluminum, loosely guided around and on center, have

been mounted without causing any compression. Peripheral, and central bearing

spindles are made with AISI 316 stainless steel.

PRESSURE-VACUUM VENT (BREATHER)

SIZE 2" 3" 4" 6" 8" 10" 12"

A 52 78 100 150 200 255 304

B 120 152.2 170 225 280 362 432

C 270 370 480 568 668 915 1060

D 205 260 375 375 375 670 670




Page 103 of 146

EN ISO 9001:2000

Vacuum Vent

Vacuum Safety Vent (Breathers)

• In atmospheric storage tanks with stable roof, where petroleum products are stored;

• Various breathers with flame arrester of different sizes and quantity,

depending on tank size and maximum number of goods in and out of tank,

should be used.

• To eliminate the happening of vacuum while discharging of tank

• In expulsing of the excess oxygen to atmosphere, which appears during good

entry to tank, in the most cost-efficient way

• In getting rid of vacuum and pressure that caused by temperature difference

between day and night, and air temperature variation, without corrupting tank

safety

• These vents, minimize tank shrinkage, and reduce economically air pollution,

are useful for atmospheric ecological equilibrium.

Technical Specifications:

They are generally manufactured in sizes of 2”, 3”, 4”, 6”, 8”, 10”, 12”




Body Material:

Body Material is rust resisting aluminum cast that do not spark due to friction and


Other materials may be used in the event of special orders.




Page 104 of 146

EN ISO 9001:2000

Clacks:

Clacks are sections, where breathing occurs and which are likely to be destructed by







Bearing in Clacks:

Caterpillar of clacks is loosely guided around, and on center. Spring is not used.


occur.

Connecting Flanges to Tank:

Connecting section’s design is mounted to flanges compatible with ASA Class 150.

They may be used in other norms on request.

VACUUM VENT (BREATHER)

SIZE 2" 3" 4" 6" 8" 10" 12"

A 52 75 100 150 200 155 304

B 120 125 170 225 280 362 432

C 250 350 450 550 650 890 1000

D 100 110 165 165 165 295 325




Page 105 of 146

EN ISO 9001:2000

Pressure-Vacuum Vent with Humidity Arrester This vent is to be used, as in base and mineral oil tanks, in case that air penetration

to the tank is undesired. Its difference, from ordinary pressure, is silikogel box

mounted to the air penetration mouth on the bottom vacuum section.

This way, since the air pass through silikogel when entering to the tank, air leaves its

humidity. The silikogel must be replaced in certain time ranges.

Flame Arrestor Flame arresters are manufactured as line and (like pipeline end and on-tank exit),

and interline.

They may be manufactured as flange on both of its ends, and also as a flat on one

of its ends.

Flame arrester unit is in the box and “Crammed Ribbon” type having wholly

changeable characteristic, and manufactured by stainless steel ribbon. The porous

effective cross section of flame arrester unit is less than fire extinguishing diameter

necessary for “air/benzene steam” mixture. Standard Quenching Diameter is

0.75mm.

Total free passing area is longer than the flame arrester’s diameter area.

Generally manufactured in sizes of 2”, 3”, 4”, 6”, 8”, 10”, 12”.

Flame arrester has been manufactured with aluminum cast resistant to petroleum

steam and may be produced with any desired material in case of orders. The flat is

covered with aluminum plate, and also be manufactured with aluminum cast.




Page 106 of 146

EN ISO 9001:2000

Connecting flanges to tank have been drilled in flange sizes compatible with ASA

Class 150. Drilling in other standards is also available on request.

Flame arresters are suitable for easy dismounting, and cleaning. It me be cleaned

with pressure air. It is easily surveyed during periodical maintenances. The device is

not required to be dismounted for periodical maintenance. It may be automatically

cleaned by itself with the petroleum steam that is caused by good loading.

FLAME ARRESTOR

SIZE 2" 3" 4" 6" 8" 10" 12"

A 50,8 80 100 150 200 254 304

B 108 152 170 225 280 361 431

C 165 240 310 370 420 577 727

D 370 410 690 690 690 720 720

A. Over-Tank and Pipeline End Flame Arrester

Its function is to prevent the flame that is likely to come from outside to get in pipe

during petroleum delivery.




necessary for “air/benzene steam” mixture. Its total free passing area is larger than

flame arrester’s diameter area.

It may easily be cleaned with pressure air. The status of filter may easily be seen

during periodical maintenances, so there is no need for dismounting. It is placed

under a flat, and its perimeter is under protection with a perforated sheet that

prevents dust, and dirt to penetrate.




Page 107 of 146

EN ISO 9001:2000

B. Inter-Pipeline Flame Arrestor This kind of flame arrester is used on inter pipelines, and prevents flame penetration

during liquid flow from a pipe to another one


changeable characteristic, and manufactured by stainless steel ribbon. The filters

may easily be removed, and cleaned with pressure air. The status of filter may easily

be seen during periodical maintenances.

Pressure-Vacuum Vent with Flame Arrester In atmospheric storage tanks with stable roof, where petroleum products are stored;

- To eliminate the happening of vacuum while discharging of tank

- In expulsing of the excess oxygen to atmosphere, which appears during good

entry to tank, in the most cost-efficient way

- In allowing the air to penetrate tank from atmosphere

- In getting rid of vacuum and pressure that caused by temperature difference

between day and night, and air temperature variation, without corrupting tank

safety

- Various breathers with flame arrester of different sizes and quantity

depending on tank size, and maximum number of goods in and out of tank

are used

- These vents, minimize tank shrinkage, and reduce economically air pollution,

are useful for atmospheric ecological equilibrium

For Fire Protection:

- It prevents the flame, which may come from outside to penetrate the tank

(with its special flame arrestor)

- It is generally suitable to mount two pressure-vacuum vent with flame arrester

to one tank whatever their sizes

- It complies with NFPA-30 regulation book, which determines combustible

fluids storage instructions.




Page 108 of 146

EN ISO 9001:2000

Technical Specifications:

Generally manufactured in sizes of 2”, 3”, 4”, 6”, 8”, 10”, 12”.




Flame Arrestor Section:




necessary for “air/benzene steam” mixture. Its total free passing area is larger than

flame arrester’s diameter area.

Flame arresters are suitable for easy dismounting, and cleaning. It me be cleaned

with pressure air. It is easily surveyed during periodical maintenances.

It automatically cleans itself during tank’s conditioning, and is generally used

together with Pressure-vacuum security vent. It is, apart from the other one, under a

flat to prevent dirt, and dust to penetrate and under protection with a perforated

sheet.

PRESSURE-VACUUM VENT WITH FLAME

ARRESTOR (BREATHER)

SIZE 2" 3" 4" 6" 8" 10" 12"

A 52 78 100 150 200 255 304

B 102,5 152,5 170 225 280 362 432

C 280 375 485 585 685 950 1750

D 410 438 805 805 805 1080 1220




Page 109 of 146

EN ISO 9001:2000

Gage Hatches A-Gage Hatch (Type-Without Lock) -May be opened when pressed its pedal by hand or foot, and closed when

released

-It acts as discharge vent at in-tank pressure of 50 mmss

B. Gage Hatch (Type-With Lock)

It is the preferable type for checking of in-tank good, evaporation loss – when left

open, or fire protection.

Specification of Both Devices

-All the parts are made of spark-proof materials.

- The material of body, clack and clack holder pedal is aluminum.

- Clack diaphragm is resistant to petroleum steam - It does not leak petroleum steam when closed - Flanges, which connect to tank, are manufactured according to ASA Class

150 - All devices are tested in our factory, and no adjustment is required in places

where mounting will be practiced.

GAGE HATCHESSIZE 4" 6" 8"Amm 100 150 200Bmm 160 170 170Cmm 170 225 280Dmm 13 14 14Emm 200 240 270

Gage Hatch Normal Type-Without Lock

GAGE HATCHES SIZE 4" 6" 8" A 100 150 200 B 160 170 170 C 170 225 280 D 13 14 14 E 200 240 270




Page 110 of 146

EN ISO 9001:2000

As shown in the picture, the gage hatch has been designed in a way to be opened

by foot, and it closes automatically when released after measuring. Therefore, the

hatch will not left open even in case of inattentiveness. Since contact surface of the

hatch are reinforced with oringles, no leaking is concerned. The hatch has been

designed not to cause sparks due to material beat, and manufactured with aluminum

cast.

The hatch has been made of AISI 316 quality stainless steel in order to avoid non-

operation of articulation due to petroleum steam, and weather conditions.

Connecting sections to tanks have been designed in a way to be mounted to flanges

compatible with ASA Class 150. It may be produced in other norms on request.

It has been manufactured in sizes of 4”, 6”, 8”.

Gage Hatch Type-With Lock As shown in the picture, the gage hatch has been designed in a way to be opened

by foot, and it closes automatically when released after measuring. Therefore, the

hatch will not left open even in case of inattentiveness. Since contact surface of the

hatch are reinforced with o’ringles, no leaking is concerned. The hatch has been

designed not to cause sparks due to material beat, and manufactured with aluminum

cast.









Page 111 of 146

EN ISO 9001:2000

GAGE HATCHES (type-with lock)

SIZE 4" 6" 8"

A 100 150 200

B 160 170 170

C 170 225 280

D 13 14 14

E 200 240 270

Gage Hatch Closed to Atmosphere This type of gage hatch is used in order to ensure pressure and vacuum not to

decrease, and to prevent steam loss during measurement.

This system consists of two sections. When the first section is opened and sample

taking device or meter mass get into it, the upper cover closes. The second section

opens, then sample taking devices, and meter mass are backed off into the tank. In

this way, the system is not opened to atmosphere.

Same process is repeated during taking back. It prevents worker’s face not to be

exposed on steam that allows healthy measurement, and sample taking.

The device’s material is spark-proof aluminum cast. No leaking is concerned due to

cover taps surfaces reinforced with teflon o’ringle.









Page 112 of 146

EN ISO 9001:2000

Menhol Type Gage Hatch Tank Height Gauges Tank Height Gauges Units:

1. Stainless Steel Float (1)

2. Rustless Guy Rope (2)

3. Tank Passing Unit (imperviousness) (1)

4. Brass Roller (3 tk)

5. Indicator Rope (1 tk)

6. Steering Pointer (1)

7. Fixed Gauge Chart

8. Spring Loaded Guy Rope Element (1)

Floating Absorption Branch It is a device that is for use to draw fuel from a place near the surface of content, and

in order not to absorb draft in tanks, where fuels such as aircraft fuel and Jet-A1 are

stored.

Internal Floating Roof It is used in tanks where petroleum evaporation level is high. It is also used in

naphtha, and benzene tanks. It has a float over the petroleum stored. It raises and

warps down together with fuel. No evaporation is possible.

A Type-With Tube

B Sandwich Panel Type

C. Special Beehive Type

Tank Thermometer Thermometers are protected in a pipe made of bronze material. They enable taking

measurements by dangled into tank through gage hatches.

While dangling the device into the tank, protection pipe closes does not let glass

broken. Its bottom bulb lets to keep the heat for a certain time.




Page 113 of 146

EN ISO 9001:2000

Cathodic Protection for Tanks Most of the tanks face fast corrosion problem because of seawater penetration. In

order to get rid of such problem, painting of the inside surface is required; also

internal cathodic protection should be procured. Although the outer bottom of tank

lay just on pitch surface, its cathodic protection is strictly required. Such protection is

practiced in two divers methods:

1) Galvanic Anode System (for internal part)

2) Outer Current-Originated System (for outer bottom)

A. Internal Cathodic Protection

Although salt water comes together with petroleum, products are thrown out during

loading of these tanks. They have corrosiveness impact.

Galvanic anodes (dual types) are primarily used in petroleum storage tanks. These

are, in brief: Mg Anode (Az-63), Mg Anode (HpMg), and Zn Anode, Al-Indium alloy

anodes.

Anodes are to be calculated according to status of tank.

B. External Cathodic Protection for Tank Bottoms

Petroleum storage tanks face often corrosion due to corrosive characteristic of outer

bottom of under and on ground tanks. Galvanic anode protection is applied, but if the

current need is high, outer current-originated cathodic protection should be

implemented.

Galvanic Anode System Impressed Current System

Mg Anode (Az-63) Fe-Si Anode

Mg Anode (HpMg) Pb-Ag-Sb Anode

(Baggy) Ti-Anode with Mixed Oxide Pot

Ti-Anode with Ceramic

Graphite Anode




Page 114 of 146

EN ISO 9001:2000

Fuel Oil Tank Bottom Serpentines Fuel Oil Tank Output Stub Heaters It is a heat exchanger, which facilitates fuel flow through pipeline increasing its heat

during the transfer of fuel heated in tank.

PPPIIIPPPEEELLLIIINNNEEE CCCOOONNNSSSTTTRRRUUUCCCTTTIIIOOONNN

Accessories of Pipeline

I. Pipes and Pipeline Laying Occupations

II. Joints and Flanges

III. Cathodic Protection for Pipeline

IV. Isolation of Pipeline

V. Heat Exchanger

VI. Valves-Check Valves-Bypass Valves

VII. Blended Type Stoppers

VIII. Pumps

IX. Pipeline Flow Surveillance System

X. Pig Receiver and Launcher Manufacture & Mounting

XI. Visual Pig Monitoring Apparatus

Pipelines and Tabulating Occupations In compliance with the handled project, pipes of suitable sizes are to be laid together

with all its accessories ranging from port to main storage tanks, from storage tanks

to tanker loading islands.

In addition, lines of tank cooling, and foam launching system are to be provided.




Page 115 of 146

EN ISO 9001:2000

Joints and Flanges These are used in pipelines compatible with the standards.

Filters Filter body is made of steel material (may also be made of rust resisting and bronze

material on request). Filter element is manufactured with stainless steel in various

meshes, and sizes.

Filter is removable, and may be cleaned. It is replicable with another new one.

Cathodic Protection for Pipeline It is well known that all pipes, which are laid underground and beneath seawaters,

corrode due to atmosphere, soil and/or material going through pipes. It has been

understood that strict protection of our pipes against corrosion is sufficient after

implementing appropriate coating and painting methods, and such protection would

only be sufficiently possible if a good cathodic protection has been ensured with a

scientific study. Some serious preliminary studies are required before preparing

cathodic protection project. These are:

- Ground-related studies

- Pipe-related studies

- Environment-related studies

After all necessary data are collected; type of protection system is decided. We can

present these systems under two main groups.

1) Galvanic Anode System

2) Impressed Current System




Page 116 of 146

EN ISO 9001:2000

Above-mentioned systems can be propped according to types of anode to be used

in each of said method.

All the calculations are to be carefully made and implemented after determining sort

of Cathodic Protection.

Isolation of Pipeline This method is implemented to prevent current to jump over undesired sections.

Flanges and bolts that are used in pipe joints are to be isolated. Flange isolation is

procured with an isolator gasket placed between two flanges.

Contact bolts isolation is enabled by slipping a rope, which narrows with heat, over

the bolt.

Placing special teflon, and isolator places will provide full isolation.

Heat Exchangers They are manufactured for various different purposes. Exchangers are produced

according to its projects. Special exchanger pipes are used for this purpose, and

these do not easily cracks.

Valves-Check Valves-By Pass Valves By-pass valves are manufactured in three different sizes, and implement by-pass to

prevent excess pressure in pipelines. Its operating system is made of stainless steel,

and outer surface is coated.




Page 117 of 146

EN ISO 9001:2000

Blended Type Stoppers

These stoppers severe ties between two pipelines in line ends. Stoppers may be

produced of steel materials, and in diver sizes.

Eight profiles, which ensure opening of line in first position, close the line in second

position, and allow no leaking.

Pipeline Flow Surveillance System This system is mounted output stub, on tank, and used for use to survey fuel flow.

Its body is made of aluminum material (may be produced with bronze and stainless

steel on request). Its surveillance glass has a thickness of 15 mm.

It can be cleaned by opening its upper cover without breaking the glass, and the

upper cover can be closed again. Capacity can be roughly monitored during

charging by means of hinged plate put inside. Its plug for taking out sample is

available below. Sample may be taken out by switching its vane.

Pig Receiver and Launcher (Manufacture and Mounting)

This is used to remove fuel dump in the pipelines. It is manufactured in various

different sizes depending on pipeline’s diameter.

Pigs that are put in pipeline pass through the pipelines with pressure caused by

pressure vanes, and manually opened. Same products may be used as receiver on

other end of the pipelines.




Page 118 of 146

EN ISO 9001:2000

Visual Pig Monitoring Apparatus

This apparatus monitors pig passing in pipeline, and determine whether it passed

from this point or not.

SSSTTTOOORRRAAAGGGEEE IIISSSLLLAAANNNDDD CCCOOONNNSSSTTTRRRUUUCCCTTTIIIOOONNN

I. Assembling and Construction of Pipeline

II. Telescopic Ladder for Storage Island Tanker Descending

III. Manufactured, Assembling, and Dressing of Canopy

Assembling and Construction of Pipeline

This unit procures that fuel coming from tanks can be loaded into tankers in the most

suitable manner. They are manufactured to enable loading from above and bottom.

Telescopic Ladder for Storage Island Tanker Descending It is used descend from storage island platform on the tanker. It can be set up when

ascending over the tanker. Other times, it can be folded, and be used as railing

around storage room. Its steps are made of aluminum, and are designed as a

portable, easily usable ladder. It provides easy ascending opportunity to tankers of

different sizes.

Manufactured, Assembling, and Dressing of Canopy ERGIL MAKINA manufactures canopy that is stated in appropriate projects.

Assembling of these canopies is made on area.




Page 119 of 146

EN ISO 9001:2000

CCCAAATTTHHHOOODDDIIICCC PPPRRROOOTTTEEECCCTTTIIIOOONNN

Design & Project Work - Petroleum Pipeline

- Water Pipeline

- Port and Quay Legs

- Pontoons and floats

Petroleum storage tank are protected against corrosion

A serious preliminary design work is required in projecting works. These works are

as follow:

- Ground-related studies

- Pipe-related studies

- Environmental-related studies

Following a serious and detailed preliminary study, projecting works will proceed by

means of data collected in preliminary study.

Cathodic Protection Materials Manufacture and Providing A Anode Manufacture

• Indium-Aluminum Alloy Anode

• Magnesium Anode

• Silicon Iron Anode

• Zinc Anode

• Variety of Special Anode

• Shring Cable

B. Test Boxes Manufacture

C. Line Marker Manufacture

D. Transformer Rectifier Unit Manufacture

E. Deep Well Cover

F. Reference Electrode




Page 120 of 146

EN ISO 9001:2000

Cathodic Protection Implementation This plant has been designed to produce mineral oils of desired capacity. It is used

to manufacture of ketyis and autoclave

MMMIIINNNEEERRRAAALLL OOOIIILLL PPPRRROOODDDUUUCCCTTTIIIOOONNN PPPLLLAAANNNTTT

A. Motor Oil Production Plant

B. Grease Production Plant

C. Special Oils Production Plant

LLLPPPGGG SSSYYYSSSTTTEEEMMMSSS A. LPG Pressure Decreasing, Measurement and Restriction Stations (SKID

TSEK.35 1402/851)

B. Isolated Coupling and Isolated Flanges

D. Cathodic Protection for LPG Pipelines

E. Laying of LPG Pipelines

F. LPG Stations Responsible Controller.

SSSEEEAAA TTTAAANNNKKKEEERRR MMMAAATTTEEERRRIIIAAALLLSSS

A Tanker Type Pressure Vacuum Vent (Turkish Lloyd Cert. No. 241297)

B Tanker Type Pressure Vacuum Vent with Flame Arrestor

C Cathodic Protection for Tankers

• Anode Manufacture

• Impresed Current Cathodic Protection

• Tanker-Related Special Manufactures

EEEXXX---PPPRRROOOOOOFFF EEELLLEEECCCTTTRRRIIICCCAAALLL MMMAAATTTEEERRRIIIAAALLLSSS




Page 121 of 146

EN ISO 9001:2000

SECTION -13

OOOUUURRR VVVEEEHHHIIICCCLLLEEESSS




Page 123 of 146

EN ISO 9001:2000

NO ENGINE INSTRUMENT and FACTORY CAPACITY QUANTITY

1 FACTORY – İKİTELLİ 2800 M2 CLOSED AREA 2 FACTORY – BAYRAMPAŞA 600 M2 CLOSED AREA 3 VAN 2 UNIT 4 TRUCK 1 UNIT 5 CAR 8 UNIT 6 TRUCK CRANE 1 UNIT 7 BULLDOZER 1 UNIT 8 ASSEMBLING CRANE 12 UNIT 9 EXCAVATOR HYDRAULIC 2 UNIT

10 COMPRESSOR 1 UNIT 11 STATIC KONTEYNER 6 UNIT 12 PERIPATETIC KONTEYNER 2 UNIT 13 HYDROSTATIC TEST EQUIPMENT 2 UNIT 14 HOLIDAY DETECT 2 UNIT 15 DRENAJ PUMP 350 M3/H 16 BENDING PIPE MACHINE 1 UNIT 17 MANTAJ KELEPAT 40" 18 CUTTING ASPHALT MACHINE 2 UNIT 19 ELECTRICAL CUTTING 2 UNIT




Page 124 of 146

EN ISO 9001:2000

NO ENGINE INSTRUMENT and FACTORY CAPACITY QUANTITY

20 ELECTRICAL DRILLING 2 UNIT 21 FULL TANK MANUFACTURE APPARATUS 12 SET 22 BENDING SHEET IRON CYLINDER Ø 2200 MM 2 SET 23 ARGON WELDING MACHINE 450 A 2 SET 24 ELECTRICAL WELDING MACHINE 450 A 48 SET 25 OXYGEN WELDING SET 12 SET 26 MEASURE EQUIPMENT OF THICKNESS COAT 0-1500 M 2 SET 27 PLANYA TOOLS 65 'lik 3 UNIT 28 BORING TOOLS 3 UNIT 29 LATHE 2.5 - 3 - 1.5 METER 3 UNIT 30 GRINDING TOOLS (SURFACE) 450X750 2 UNIT 31 GRINDING TOOLS (CYLINDER) Ø 250X750 M 2 UNIT 32 AUGER TOOLS Ø 13- Ø 32 12 UNIT 33 RADIAL AUGER TOOLS Ø 32 2 UNIT 34 LARGE DIAMETER HORIZONTAL LATHE Ø 5000 2 UNIT 35 BORVERK TOOLS Ø 63 M 2 UNIT 36 WATER PUMP 1 UNIT 37 KOMPACTOR 1 UNIT 38 ALUMINIUM CASTING ROOM 1 UNIT

KerimALTUNERGİL Genel Müdür




Page 125 of 146

EN ISO 9001:2000

NO ENGINE INSTRUMENT and FACTORY CAPACITY QUANTITY 39 ECCENTRİK PRESSING MACHINE 60 TON 2 UNIT 40 ECCENTRİK PRESSING MACHINE 40 TON 2 UNIT 41 ECCENTRİK PRESSING MACHINE 25 TON 2 UNIT 42 HYDRAULIC PRESSING MACHINE 150 TON 6 UNIT 43 PLASTER TOOLS Ø 750 MM 4 UNIT 44 GUILLOTINE SCISSORS 2200 MM 2 UNIT 45 SPREAD CABLE TOOLS 2 UNIT 46 GENERATOR VARIOUS 4 UNIT 47 WATER PUMP WITH PRESSURE 1 UNIT 48 DIESEL WELDING MACHINE 1 UNIT 49 PE WELDING MACHINE(ELE.FUSION) 1 UNIT 50 PE WELDING MACHINE(BUTT FUSION) 1 UNIT 51 PE WELDING CLIPS VARIOUS DIAMETERS 2 SET 52 PIPE CLIP 1 UNIT 53 TERMOMETER 1 UNIT 54 GAS DETECT 1 UNIT 55 HYDRAULIC SUFFOCATING 1 UNIT




Page 126 of 146

EN ISO 9001:2000

SECTION -14

FFFIIIRRREEE FFFIIIGGGHHHTTTIIINNNGGG EEEQQQUUUIIIPPPMMMEEENNNTTT




Page 127 of 146

EN ISO 9001:2000

AAACCCCCCEEESSSSSSOOORRRIIIEEESSS OOOFFF FFFIIIRRREEE EEEXXXTTTIIINNNGGGUUUIIISSSHHHIIINNNGGG SSSYYYSSSTTTEEEMMMSSS

I. Foam Launching Systems

A. Foam Mixing Devices

a. Vacuum System

b. Coercive System

B. Foam Makers

C. Foam Fuse

D. Foam Springs

E. Foam Launching Cannon

F. Foam Storage Tank

II. Tank Cooling System

A. Tank Surrounding Cooler Spring

B. Tank Roof Cooler Spring

C. Fire Hose Records

D. Special Check Valve of Sea Water Receipt (for Fire Water Pumps)

Foam Launching Systems A. Foam Mixing Devices

While pressure water pass under foam fluid tank, these devices procure to inject

foam fluid into water in certain proportion.

B. Foam Makers

It is made of aluminum-stereo or stainless steel pipe to generate foam. It combines

water, fluid foam, and air to produce foam. It conveys this foam-to-foam fuse.

C. Foam Fuse

It pours foam. After foam coming from foam maker reach a certain rate of pressure,

glass breaks and foam is poured into tank.




Page 128 of 146

EN ISO 9001:2000

It may have different sizes compatible with tank dimensions. It is mounted to side

surface of tank. In-tank design is made in order to let foam reach fuel surface in the

fastest way.

D. Foam Springs

It is used to squirt foam on ceiling of storage rooms. It distributes foam from foam

maker with raining system.

E. Foam Launching Cannon

It is designed to launch foam on petroleum stored in the tank.

It may function as fixed or portable device. Its monitor has two nozzles in a way to

launch water and foam. Its monitor is manufactured in convertible structure foam

water to foam, or foam to water without cutting water flow and designed as a

manually controlled device. Its monitor capacity is 1500-3000 lt/min.

Its monitor may pivot 360, and incline ahead, and behind 60-70. it may have a

system of two wheels and braking equipment as well as fixed system.

F. Foam/Fluid Storage Tanks

Foam is preserved in a tank in places where mixing device and foam maker are not

used. Foam in tank prevents sedimentation of fuel due to its mixing characteristic.

Tank is painted with epoxy dye, and made of stainless steel. An appropriate

pressure vacuum vent is available over fluid in order to prevent air contact.

Tank Cooling System Petroleum storage tanks should be equipped with foam launching systems for fire

protection. Foam launching systems consists of mixing makers, foam makers and

fire fuse.




Page 129 of 146

EN ISO 9001:2000

Foam fuse is not mounted on tank roof but on tank side 20 cm below its roof. So, if

tank roof is removed, foam launching may continue.

Tank cooling system is provided by springs placed on ends of pipes laid around the

tank.

Water flowing in a appropriate number of springs allows tank cooling. A suitable

spring system should be set up on tank roof. In this way, tank is cooled to prevent

evaporation in cases of fire dangers and in warm weathers.

A Tank Surrounding Cooler Springs

It is used as a tank side water-cooling system, which is mounted on tank

surrounding.

These springs spray the water taken from pipeline to procure tank cooling.

B Tank Roof Cooler Springs

They are mounted on tank roof as a tank cooling system.

They enable cooling of upper part of tank by practicing raining system on tank roof.

C. Fire Hose Records

These hoses are made of aluminum. They are compatible with TSE (Turkish

Standard Institute) standards.

D Special Check Valve of Sea Water Receipt (for Water Pumps)

Absorption pipe, and check valve of this water pump are made of bronze material or stainless steel. It should be ready to serve continuously in order to benefit from seawater in casting plants - located on coastline.




Page 130 of 146

EN ISO 9001:2000

FIRE PROTECTION ACCESSORIES FOR PETROLEUM STORAGE TANK

FOAM LAUNCHING CANNON Foam launching Cannon is designed to launch the over of storage tanks. It can be used mobile or stationary. It has two nozzle, one of the nozzle for just water, the other one to launch foam. The nozzles are made by aluminum and are resistant to corrosion. Screen Capacity : 1500 - 3000 lt/min. It has manometer to indicate the flowing pressure. The screen can be rotated 360 degrees horizontally , 60-70 degrees vertically The Screen has two wheel and brake system. Spare parts can be supplied easily, because it is manufactured seriously. Also it can be carried easily ,periodically at each six months

FOAM DISTRIBUTER

FOAM NOZZLE

FOAM SPRING

TANK COOLER SPRING

FOAM NOZZLE HEAD




Page 131 of 146

EN ISO 9001:2000

MIXING DEVICES 3" 750 liter/minute 4" 1500 liter/minute

FOAM MAKER 3" 750 liter/minute 4" 1500 liter/minute

Materials: The Aluminum that resistance to products and steam of petroleum, AISI 316 stainless steal, ambient-Teflon gasket, cadmium covered bolts Connection to Tanks: Connection is designed according to standard of ANSI, API 150.

FIRE FUSE For Horizontal Petroleum Storage Tank (4"~6" ) It is designed according to the size of storage tank.

Sahara Type Boxes of the Fire Protection System




Page 132 of 146

EN ISO 9001:2000

SECTION -15

OOOUUURRR FFFIIIRRRMMM RRREEEFFFEEERRREEENNNCCCEEESSS




EN ISO 9001:2000

REFERENCES

NO NAME OF FIRM 1 ACIBADEM SAĞLIK HİZMETLERİ A.Ş. 2 ALARKO-ALSİM A.Ş 3 ALKAN İNŞ.TAAHHÜT VE TİC.A.Ş 4 AMBARLI DEPOLAMA HİZMETLERİ. 5 AMYLUM NİŞASTA SAN.VE.TİC.A.Ş. 6 ATAŞ ANADOLU TASFİYE HANESİ A.Ş. 7 AYTEMİZ AKARYAKIT ORTAKLIĞI 8 BAŞER PETRO KİMYA SAN.A.Ş 9 BEYAK BEYLİ YAKIT TİC.A.Ş 10 BMS MAKİNA İNŞ.VE.MAK.SAN.TİC.LTD.ŞTİ 11 BOTAŞ A.Ş 12 BÖLÜNMEZ PETROLCÜLÜK A.Ş 13 BP AKARYAKIT ORTAKLIĞI 14 BP GEMLİK AKARYAKIT ORTAKLIĞI 15 BRİSA BRİDGESTONE SABANCI LASTİK




EN ISO 9001:2000

16 BTC KONSORSİYUMU 17 CACA MAKİNA SAN.VE TİC.LTD.ŞTİ. 18 ÇAMSAN AĞAÇ SANAYİ.TİC.A.Ş 19 ÇEKİSAN DEPOLAMA HİZMETLERİ. 20 ÇİĞDEM İNŞAAT SAN.TAAHÜT A.Ş. 21 ÇİLTUĞ ISI SANAYİ TİCARET A.Ş. 22 ÇİMTAŞ A.Ş. 23 DENİZ TANKER İŞLETMECİLİĞİ 24 DENMAR DEPOCULUK NAK.TİC.A.Ş 25 DESA MÜH.VE.YATIRIM MALL.A.Ş. 26 DOĞAN YANGIN SÖNDÜRME SAN.A.Ş 27 DOSTEL İNŞAAT TAAH.VE.TİC.LTD.ŞTİ 28 DÜZGİT VAPUR HİZM.TİC.A.Ş 29 EGE GÜBRE SANAYİ A.Ş 30 EMİ ELEKTRO MEKANİK 31 ENKA TEKNİK A.Ş. 32 ERDEM İNŞ.TİC.LTD.ŞTİ 33 ESEN MAKİNA SANAYİ TİC.A.Ş




EN ISO 9001:2000

34 FARUK ALKAN İNŞAAT MÜH. 35 HALİKARNAS DENİZCİLİK VE PETROL TAŞIMACILIK SAN.TİC.AŞ36 HAVATEK MAKİNA SAN.TİC.A.Ş 37 İGDAŞ 38 İSKİ GENEL MÜDÜRLÜĞÜ 39 İSTON A.Ş. 40 KALYON İNŞAAT A.Ş. 41 KIRDAR TAAHÜT VE TİC 42 KOZA TİCARET 43 KUVEYT TÜRK EVKAF FİNANS KURUMU A.Ş 44 MERCEDES BENZ TÜRK A.Ş 45 METRANS END.ÜRÜN.PAZ.LTD.ŞTİ 46 MOBİL MADENİ YAĞLAR ORT. 47 NİTROSAN A.Ş. 48 OPET PETROLCÜLÜK A.Ş. 49 ORPET GÜMRÜKLEME SAN.LTD.ŞTİ 50 ORUÇ OĞLU YAĞ SANAYİ VE TİC.A.Ş. 51 OVA ELEKTRİK A.Ş.




EN ISO 9001:2000

52 PASİFİK DENİZCİLİK NAK.LTD.ŞTİ 53 PATA MAKİNE 54 PEKER EVSER KRASNODAR İŞ ORTAKLIĞI 55 PETKİM PETROKİMYA HOLDİNG A.Ş. 56 PETROL OFİSİ A.Ş 57 POLİPORT KİMYA SANAYİ TİC.A.Ş 58 PROCTER GAMBLE TÜK.MAL.A.Ş. 59 SERVET ARAR İNŞAAT MAKİNA SAN.VE.TİC.LTD.ŞTİ. 60 SİMGE İNŞAAT LTD.ŞTİ. 61 SOYAK İNŞAAT VE TİC.A.Ş. 62 T.H.Y 63 TANKTES MAK.İMALAT MÜH.LTD. 64 TEKFEN İNŞAAT VE TESİSAT A.Ş. 65 TOROS GÜBRE VE KİMYA A.Ş 66 TOTAL OIL TÜRKİYE A.Ş. 67 TUNÇ DENİZCİLİK TANKERCİLİK DONANMA İŞTİRAKİ 68 TURCAS PETROLCÜLÜK A.Ş. 69 TURKUAZ PETROL ÜRÜNLERİ A.Ş.




EN ISO 9001:2000

70 TÜPRAŞ PETROL RAFİNERİLERİ MÜDÜRLÜĞÜ A.Ş. İZMİR 71 TÜPRAŞ PETROL RAFİNERİLERİ MÜDÜRLÜĞÜ A.Ş. KIRIKKALE 72 TÜPRAŞ PETROL RAFİNERİLERİ MÜDÜRLÜĞÜ A.Ş. İZMİT 73 TÜPRAŞ PETROL RAFİNERİLERİ MÜDÜRLÜĞÜ A.Ş. BATMAN 74 ÜNKA İNŞ.TES.SAN.TİC.LTD.ŞTİ 75 VENEDİK İNŞ.TAAH.TİC.SAN.LTD.ŞTİ 76 SHELL 77 BP 78 TOTAL 79 AL EMAD GENERAL TRADING / UAE 80 KITO / GERMANY 81 FLOWTECH MARKETING / MALASIA 82 HIGH ARCTIC / UAE 83 ARMIN GROUP / IRAN 84 ALLALAMIAH TRADING GROUP / KUWAIT 85 FOURESS GROUP / INDIA 86 SHAHIG CO. / KINGDOM OF SAUDIA ARABIA 87 KAR AVRASYA




EN ISO 9001:2000

88 LBL TRADING CO. / ISRAEL 89 PREMIUM ENERGY / PAKISTAN 90 2L DISTRIBUTION / FRANCE 91 JOTUN / TURKEY-BELGIUM 92 ALGHANEM / JORDAN 93 PUNJ LLOYD 94 TECH INTERNATIONAL 95 OGI GROUP / CANADA 96 CARGILL 97 MOMENTUM ENGINEERING 98 TEZKIM / TURKEY 99 TAM İNŞAAT / TURKEY 100 ŞÜKRÜ TÜREDİ / TURKEY 101 SÖNMEZ METAL / TURKEY 102 ES ENDÜSTRİ / TURKEY 103 CİLTUĞ A.Ş. / TURKEY




Page 138 of 146

EN ISO 9001:2000

SECTION -16

PPPRRROOODDDUUUCCCTTT DDDEEETTTAAAIIILLL




Page 139 of 146

EN ISO 9001:2000

NO PRODUCT OR DETAIL DETAIL NO 1 ALGORITMA ARITHMETIC OF PRESSURE VAKUUM

VENT CAPACITY -

2 6” FLOATING SUCTION PIPE MAK 073/3 3 FUEL LINE FILTER MAK 052/00 4 MIX-MAKERS MYA 03/00 5 PıG RECEıVER/LAUNCHER MAK 076/00 6 2” PRESSURE VAKUUM VENT MAK 008/00 7 6” GAUGE HATCH (LOCKED) MAK 045/00 8 6” GAUGE HATCH MAK 049/00 9 6” NON-ATMOSPHERIC GAUGE HATCH MAK 061/00

10 6” FLAME ARRESTER MAK084/00 11 6” PRESSURE VAKUUM VENT MAK 011/00 12 INTERNAL FLOATING ROOF MŞT 05/00 13 ALUMıNIUM ANODE MKK07 /00 14 ALUMıNIUM ANODE TYPE CLIP KK012/1-00 15 REFERANS ELEKTROT (SEYYAR) MKK01/02 16 REFERANS ELEKTROT (PORTABLE) MKK-01/01 17 FLOW INDICATOR MAK 060/00 18 URGENT SECURITY VENT MAK 092/00 19 FOAM LAUNCHER MYA 010/00 20 CATHODIC PROTECTION OF STORAGE TANKS KKK032/00 21 FIRE INSURANCE MYA 008/00

600 MENHOL TAP MAK 075 /00




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EN ISO 9001:2000

SECTION -17

WWWEEE RRREEEPPPRRREEESSSEEENNNTTT




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EN ISO 9001:2000

SECTION -18

RRREEEPPPRRREEESSSEEENNNTTTAAATTTIIIVVVEEESSS




Please Email [email protected] For More Information About Our Agents And/Or How To Become A Representative.




Page 144 of 146

EN ISO 9001:2000

SECTION -19

BBBRRROOOCCCHHHUUURRREEESSS

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