NATIONAL IRANIAN GAS COMPANY Optimization and … · Using DEG 1.5 GPMŁW.C 92ppm Using TEG 1.5gpm...

SARKHOON & QESHM GAS TREATING COMPANYTECHNICAL & ENGINEERING SERVICES

PROCESS ENGINERINGBY: ABOLFAZL ATASH JAMEH

NATIONAL IRANIAN GAS COMPANYOptimization and Modification

of Dehydration Process in Gavarzin Gas Plant

Abolfazl Atash JamehAbolfazl Atash Jameh--Sarkhoon & Qeshm Gas Treating CompanySarkhoon & Qeshm Gas Treating Company--IRANIRAN

History of Plant

Commission of plant in 1979 at north of Persian Golf in Qeshm Island

Capacity of plant 100MMSCFD

Dehydration Solvent: TEG

Water dew point -9.5°C or water content 60.95 ppm

IGS for water content 110 mg/Sm3

Abolfazl Atash JamehAbolfazl Atash Jameh--Sarkhoon & Qeshm Sarkhoon & Qeshm Gas Treating CompanyGas Treating Company--IRANIRAN

Main Objectives of Modification

Produce On SPEC Sales Gas in Plant

Consideration of Concerns for Commissioning of CNG Station In Qeshm Island Due to High Water Dew Point of Natural Gas

ROOT Cause Survey

Process Simulation

Check Operational Equipments

Executive Simulation results

Simulation of plant with Hysys Simulator

Using DEG 1.5 GPMè W.C 92ppm

Using TEG 1.5gpm è W.C 65ppm

Water Dew Point - 3.4 °C @ DEG

Water Dew Point - 7.4 °C @TEG

Reboiler Temp @ TEG 204 °C

Reboiler Temp @ DEG max 175 °CAbolfazl Atash JamehAbolfazl Atash Jameh--Sarkhoon & Qeshm Gas Treating CompanySarkhoon & Qeshm Gas Treating Company--IRANIRAN

Results of Software

Checking Operational Equipments

Performing improving of Bubble Caps

More Supervisory on

Bubble cap installation

Local of bubble caps leakageAdding new sealing on capsAppropriate sealing on trays

Some Other TestsMetering of associated water with

natural gas 70 lit /hr

@ Design Con 1.5 m3 Water /MMSCM

@ Operation Con 0.85 m3 water /MMSCM

Analyzing of Natural gas to towers

@ Des Con C6+ =0.29% Op 0.46%

The Study of Document

n Data gathering from 1998 to 2008

Executive the result of simulation,Change of Reboiler Temperature

& Stripping Gas

Step1 from 120 to 130 °C

DEG from 92% to

STRIPPING GAS FROM

30% TO 40%

Step2 from

130 to 140 °C

DEG from 96% to

STRIPPING GAS

FROM 40% TO

from 140 to

160 °C

DEG from 98% to

Analyzer Before modification

Results of On –Line Analyser

Trend of improving in stage Final Test based on on-line Analyser

Great Achievement on November 2008

2008.11.30

2008.12.1

2008.12.2

2008.12.3

2008.12.5

15water content(ppm)

Water Dew Point(0C)

Software

water Dew point(oC)

W ater Content(ppm)

Advantages & Disadvantage of TEG TO DEG

AdvantageAdvantage

MORE D.P DEPRESSIONMORE D.P DEPRESSION

DisadvantagesDisadvantages

HIGH HEATING CONSUMTIONHIGH HEATING CONSUMTION

LOWER APPROCH OF DEGRADATION TEMP AND OPERATION TEMP(207 0C & 204 0c) (for DEG 175 0c versus 120 -160 0C)

Stripping gas Stripping gas

CONCLUSION 1

Approaching to supply on-spec

production according to Iranian Gas

Standard (IGS)

Making a safe side for Natural consumers

in CNG Stations

as fuel for cars

Reduction of maintenance

cost on pipe line

transmission of natural

gas due to be dried

natural gas.

A Potential Total

Income

($/YEAR) 67,000,000

A Short look at H/C Dew Point Modification of Sarkhoon Gas

Root Cause Survey

Software Simulation

Amount of injecting glycol was decreased about %30

Design= 3.6 m3/h Operation= 2.86m3/h

Decrease of Glycol injection to E-402

Increase of Glycol injection to Chiller (E-403)

Hydrate has been formed in final filter at dehydration unit

Software Simulation

Operational Conditions

During 24 hours one of the problems it was clear that within S- 601 (flash drum) of glycol regeneration unit increase in the fluid was in the sense that at most contraceptive flows could be

transferred from unit 3.2 m 3/hr.

Glycol injection pump pressure (P-601) has increased to 76 barg to increase the amount of glycol injection.

The whole flow of glycol has increased after making optimal amount injection to chiller and gas/gas heat exchanger to reduce output gas temperature from chiller to below -12 °C.

After the deduction every day the dew point every train is the most will equip by the lab and theamount of glycol injection was changed into considering drop pressure of heatexchanger, chiller, final filter and dew point same train and after the changes for 24 hours, maximumeffort had been done to other parameters does not change.

Survey Capacity of Glycol Regeneration Unit (Unit 600)

Then flash drum pressure have been increased during 5 days from 3.8 barg to 5.5 barg and hereby the flow could be transferred to glycol regeneration unit

have been increased from 3.4 m3/hr to 4 m3/hr.

With regard to main drop pressure in heat exchanger that prescript to increase flash drum pressure from 3.8 barg to 5.5 barg.

Then focused on drop pressure of heat exchangers package and clear that fourth heat exchanger and coil reboiler have been done decrease in flow about

0.2 m3/hr.

According to the fact that the process restriction after flash drum, entrance filters and heat exchangers of glycol regeneration package had been tested .

Comparison of H/C Dew points

2007-20082008-2009

Comparison of Hydrocarbon Dew points in times 2007-2008 and 2008-2009

CONCLUSION 2Adjust products to

concordance customers (National Iranian Gas

Company)

Decrease drop pressure in vessels

that led to the lack of filter elements replacement

To prevent NGL loss about 700 kg/MMSCMD

Decrease maintenance expenses whether filter

element replacing, unwanted maintenance of

exit analyzer and calibrating unit 400 instruments

A Potential Total Income

: ($/YEAR)

484,000,000

And Reduction CO2 Emission

8 Milion ton /year

Thank You For Attention

NATIONAL IRANIAN GAS COMPANY Optimization and … · Using DEG 1.5 GPMŁW.C 92ppm Using TEG 1.5gpm...

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