enterprise products enterprise products holdings llc · enterprise products partners l.p....
TRANSCRIPT
ENTERPRISE PRODUCTS PARTNERS LP ENTERPRISE PRODUCTS OPERATING LLC ENTERPRISE PRODUCTS HOLDINGS LLC
Enterprise (General Partner) Products
March 8 2017
7015 1520 0002 7267 0373 Return Receipt Requested
Federal Minor NSR Permit Coordinator US EPA Region 6 1445 Ross Ave Suite 1200 Dallas TX 75202
Re Enterprise Field Services LLC Lindrith Compressor Station Lindrith Rio Arriba County New Mexico Minor Modification of Permit Number R6NM-03-Rl
Dear Sir ofMadam
Enterprise Field Services LLC (Enterprise) is submitting this application for a minor permit modification to Permit Number R6NM-03-R1 which was issued on November 4 2015
AIR EMISSIONS IMPACT
The change proposed in this application involves increasing the following limits within the CUITent air permit
Page Current Limit Proposed Limit
TBATTERY 3 3739 tonsyear 10263 tonsyear
TLOADING 3 223 tonsyear 498 tonsyear
MSS 3 2500 tonsyear 3000 tonsyear
Condensate 7 20000 barrelsyear 60000 barrelsyear Throughput
The increase of emissions is explained in detail in the attached calculation spreadsheets The activities which generate these VOC emissions are the storage of condensate and loading of trucks to remove the condensate to off-site destinations
REGULATIONS IMPACT
This application has been prepared in accordance with EPA guidance The current permit page 18 paragraph 59 lists the limitations ofthe minor modification procedure as follows
5911 Do not violate any applicable requirement This application does not
5912 Do not involve significant changes to existing monitoring reporting or recordkeeping requirements in the permit This application does not
1100 LOUISIANA STREET P 0 BOX 4324 HOUSTON TX 77002-5227HOUSTON TX 77210-4324
wwltgt~enterpri6e)roductscom713381 6500
US EPA Region 6 Lindrith Compressor Station March 8 2017 Page2
5913 Do not require or change a case-by--case determination of an emission limitation or standard or a source-specific determination for temporary sources of ambient impacts or visibility or increment analysis This application does not
5914 Do not seek to establish or change a permit term or condition for which there is no corresponding underlying applicable requirement to which the source would otherwise be subject This application does not
If you should have questions or need additional infonnation regarding this application please contact Robert Havalda at 713-381-6698 or by email at nnhavaldaeprodcom or Brad Cooley at 713-381-5828
Sincerely
Robert Havalda Bradley Coole Senior Environmental Engineer Senior Mana er Environmental Permitting
bjm Attachments EPA Administrative Permit Amendment Request (Form AMEND)
Process Flow Diagram Detailed Emission Calculations HYSYS Flash Analysis TANKS 409d Output Site Gas Analysis
cc Mr Jim Lieb - Enterprise Products Operating
Tribal Environmental Contact- Jicarilla Apache Attn Ms Bonnie Braganza P E US EPA Region 6 1445 Ross Ave Suite 1200 Dallas TX 75202
Mr Cordell Tecube Environmental Protection Office Jicarilla Apache Tribe PO Box507 Dulce New Mexico 87528
Enterprise Field Services LLC Lindrith Compressor Station
Rio Arriba County New Mexico
Minor Permit Modification Permit No R6NM-03-Rl
MARCH2017
OMB Control Number Pending middot
UNITED STATES ENVIRONMENTAL PROTECTION AGENCY FEDERAL MINOR NEW SOURCE REVIEW PROGRAM IN INDIAN
COUNTRY
Administrative Permit Amendment Request (Form AMEND)
Please check box to show how you are using this form
0 Correction to a Typographical Error 0 Incorporation of More Frequent Monitoring or Reporting 11 Increase in Allowable Emissions (SEE INSTRUCTIONS) 0 Other
Use of this information request form is voluntary and not yet approved by the Office ofManagement and Budget The following is a check list ofthe type ofinformation that Region 6 will use to process information on your proposed project While submittal ofthis form is not required it does offer details on the information we will use to complete your requested approval and providing the information requested may help expedite the process Use ofapplication forms for this program is currently under Office ofManagement and Budget review and these information request forms will be replacedupdated after that review is completed
Please submit information to following two entities
Federal Minor NSR Permit Coordinator US EPA Region 6 1445 Ross Ave suite 1200 6MM-AP Dallas TX 75202 R6airpermitscmagov
For more information visit httpwww2epagovcaashypermittinglcaa-permitting-epasshysouth-central-region
A COMPANY INFORMATION
The Tribal Environmental Contact for the specific reservation
Ifyou need assistance in identifying the appropriate Tribal Environmental Contact and address please contact
R6airpermitsepagov
Company Name (Who owns this facility) Enterprise Field Services LLC
Company Contact (Who is the primary contact at the company that owns this facility) Robert Havalda
Title Sr Environmental Engineer
Mailing Address PO Box 4324 Houston TX 77210-4324
Email Address nnhavalda~rodcom
Telephone Number Facsimile Number 713-381-6698 1713-381-6811
B FACILITY INFORMATION Facility Name on the Permit to Be Amended Lindrith Compressor Station
Minor Source Permit To Construct Number Not Applicable
Date ofMost Recent Permit Action (this should be the same permit to which you are requesting the amendment) November 4 2015 (Permit Number R6NM-03-R1)
C DESCRIPTION OF THE PROPOSED AMENDMENT
Provide a nanative description ofthe requested amendment to the permit and the following
1 Why the proposed change can be made through this form (See instructions)
Enterprise Field Services LLC (Enterprise) is proposing to increase the allowable emission rate for the following emissions units
1 Increase the annual throughput for condensate tank battery (Unit ID mATfERY) from 20000 barrels per year (bbllyr) to 60000 bblsyr (fBATIERY consists of eight 454-bbl fixed roofstorage tanks)
2 Increase truck loading (Unit ID TLOAD) emissions from 20000 to 60000 bbllyr to accommodate the increased throughput from TBATTERY and
3 middot Increase Maintenance Startup and Shutdown (Unit ID MSS) emissions to accommodate the increase in the natural gas VOC content
The proposed change in gas composition will add 7298 TPY of VOCs to the facility This facility is currently and will remain a minor NSR source
2 Information presented in enough detail to document how the facility is currently operating and how it is proposed to operate A narrative description ofall ofthe facility processes along with a process flow diagram to enable EPA to understand the effect the proposed change has on emission unit or (pollutant generating activity)
The Lindrith Compressor Station is a natural gas compression and transmission facility that relteives natural gas from a gathering system and compresses that gas for transmission via pipeline The emissions units at the facility consists of three reciprocating ioternal combustion engines (RICE) that drive tbe compression units (Unit IDs A-01 A-02 and A-03) the emergency RICE generator (Unit ID EMERGEN) emissions from engine starts compressor blowdowns vessel and piping blowdowns and pipeline pigging activities including the pipeline pigging location (Unit ID MSS) fugitive emissions from valves flanges compressors pumps etc (Unit ID FUGVOC) eight 454-bbl fixed roof condensate storage tanks (Unit ID TBATIERY) and condensate truck loading (Unit ID TLOAD) There are no physical changes to the emission units in this permitting action A process flow diagram is included in the attachments
Page2 of6
3 Emissions calculations and all supporting data necessary to establish the proposed post-change allowable emission limits The requested information must be provided for each emissions unit (or pollutantshygenerating activity)
Attachment 2 contains emissions calculations tables and supporting documentation for each change requested
4 The proposed changes to be made to specific terms and conditions ofthe permit A redlinelstrike out version of the permit may be used for this purpose
Enterprise is proposing the following changes to the specific terms and conditions of the permit
Page Current Limit Proposed Limit
TBATTERY 3 3739 tonsyear 10263 tonsyear
TLOADING 3 223 tonsyear 498 tonsyear
MSS 3 2500 tonsyear 3000 tonsyear
Condensate 7 20000 barrelsyear 60000 barrelsyear Throughput
5 The fillo owmg a ewt ac 1 y-wt e tnlSSlOll 1ma est bl th F irt d E Esf t
Pollutant Pre-Change AUowable Post Ch~ge Allowable Emissions (tpy) Emissions (tpy)
PM
PMto
PM2s
so2
NOs
co
voc
Pb
Fluorides
H2S04
H2S
TRS
291
291
291
426
6629
10257
13836
0
NA
NA
NA
NA
291
291
291
426
6629
10257
21134
0
NA
NA
NA
NA
PM - Particulate Matter PM10 - Particulate Matter less than 1 0 microns in size PM2s - Particulate Matter less than 25 microns in size S~ - Sulfur Oxides NOx -Nitrogen Oxides CO - Carbon Monoxide VOC - Volatile Organic Compound Ph - Lead and lead compounds Fluorides - Gaseous and particulates H2S04 - Sulfuric Acid Mist H2S - Hydrogen Sulfide TRS -Total Reduced Sulfur RSC - Reduced Sulfur Compounds
RSC NA NA
Page3 of6
COMPRESSED NATURAL GAS TO PIPELINE
GASCOQER
EPHA-()1
EPHA-02 GAS TO
COMPRESSION
------------ EPNA-03
CATERPILLAR 36121pound
2ND STAGE GAS
bull bull INLET SAPERATOR COMPRESSORSINLET GAS CONOENSAlE bull I SWG CATCHER
EPNFUGOC I bull UQUDS FROM INTERSTAGE
EPNMSS COOLERSSCRUBBERS
PIPING EPN BATIERY COMPONENTS
NA~AL GAS FROM bull I tISS EVENTS
STA110N BLOYlaquolOWN VENT 88881 I CONDENSAlE 1RUCK LOADINGeeeer-H
CATERPILLAR 3612LE
CATERPILLAR 3612tE
454-bbl TANK BATlERY
DatePROCESS FLOW DIAGRAM Designed By WY 610916
LINDRITH COMPRESSOR STATION Drawn By WY 60916 I Figure NoENTERPRISE FIELD SERVICES LLC Checked By LDC 610163631170 -10708664 Approved By lOC 610116 I Sheet of1 1LINDRITH NEW MEXICO
Table B-1 Project Emissions Summary (Criteria Pollutants) from Increased Condensate Throughput Lindrith Compressor Station Enterprise Field Services LLC
ID EmlniON
loune Deecrlpllon YOC HAh
I Conctennt -jThroughput
tPv ~ BbfV_r I Limits In Currnt Permit Number R6NM-03-R1
TBATTERY Tanks Condensate Storage 3739 107 20000
TLOAD Truck Loading Truck Loading 223 007 20000
MSS MSS Maintenance Startup ShutdoMl
2500 064 nla
Total 6462 178
Proposed Pennit Umlts
TBATIERY Tanks Condensate Storage 10263 132 60000
TLOAD
MSS
Truck Loading Truck Loading
MSS Maintenance Startup Shutdown
Tote -------shy -shy -
498
2998
13759 -
014
059
205
60000
na
Table B-2 Tank Emissions from Increased Condensate Throughput Lindrith Compressor Station Enterprise Field Services LLC
ID lllitarW StonKI Ttnk
Caplclly (OIIoM)
No of ~per
~ ~ -- -middot _ -~middot~
VOC Annul en-lionS Rites
TANKS40 TOUIIVOC AMivrhshy
TANKS40 TotaiVOC
-ltnv
Flab EmiNiona
rltBWmiddot middot
OVerall
~~~ T1 Condensate 18900 1887 421056 211 1072 1213
T2 CondenNia 18900 1667 421058 211 1072 1213
T3 Condenstte 18900 Hl87 421058 211 1072 1283
T4 CondenMte 18900 1667 421056 211 1072 1283
TS Condensate 181100 1887 421056 211 1072 1283
T8 Condensate 18900 1687 421056 211 1072 1283
T7 Condensate 18900 1667 421058 211 1072 1283
T8 Condenlft 18900 1887 421056 211 1072 1283
Total 1amp1200 33184A8 1184 8579 10263
(1) See TANKS 40 Report Results (2) Gasoline RVP 7 properties are used to estimate condensate emissions (3) See HYSIS Flash Analysis Flash emissions =Condensate Throughput x (VOC Mass Flow lblhr x 24 hr I Std Ideal Liq Vol Flow bbllday) (4) Speciation method below Is the same as used for the renewal application for current Permit Number R6NM()3-R1 (5) Refer to Lindrith Compressor Station_Wmter Case 3hsc analysis dated 712812016
Speclated Eml8slons Based on Aspen Ana_~ Is of vapor~t ase (normalized by deleting all non-voc compounds)
Comfound ~eiGht
Non HAPs 987180 10131 n-Hexane 12720 131 Benzene 00050 001 Toluene 00030 000
E 00010 000 Xvlenes o_001o 000
HAPs TOW 128 s
Table B-3 Truck Loading Emissions from Increased Condensate Throughput Lindrith Compressor Station Enterprise Field Services LLC
Basis Emissions calculated based on loading loss factors from EPAs AP-42 Table 52-1 Section 52 June 2008 VP based on maximum expected liquid temperature for the short-term and annual average liquid temperature for the annual basis
Product Loading Type tiN
bull Short-Term
MaxVP
Ant1UI
AwrageVP middot _ ~-middotmiddot
middotmiddot -
SaturatiOn Factor S -shy
-bullmiddot__ middotfmiddot middot y -ShortmiddotTerm Loading Annuli Loedlng LOM
Lou Factor Factor _ middot middotmiddot ~ middot
nvOughpUt
(981r) (gallyr) lblhr tpy
J
Condensate Submefged 6800 524 404 06 48398 1b1ooo gal 39496 lb1000 gal 18000 I2520000 8712 498 I
Totals 2520000 8712 498
Notes Errisslons 8AI b~slld on the loading tosses equation Tom EPAs AP~2 Section 2 5th Edition June 2008 Equation 1 L =1248 x S x P x MI T
L Loading Losses lb1000 gallons S bull Saturation Factor see Table 52-1 in AP-42 Section 52 P s True vapor pressure psia M= Molecular weight olvapors lbllb-mol T = Temperature of bulk liquid loaded R (F + -46 -524
____ shy -middotmiddot- - - -middotmiddot middot middotmiddotmiddot-bull1middot middot- -middot ~~~ -normalized by deleting all non-voc compounds) bull~011pound
Non HAPs
middot wetgm __
971343 middotllllnT
8462
483
___
n-Hexane 22491 196 011 Benzene 03333 029 002 Toluene 02833 025 001
Ethlybenzene 00000 000 ooo Xylenes 00000 000 000
Total 10000 bull ~ middotshy bullbull 1 middot bullmiddot ~ bull middot __
VOCTotal 10000 8712 498 HAPs Total - 287 _____150 014
1) Speciation method is the same as used for the renewal application for current Permit Number R6NM-03-R1 2) All no~HAPs assumed VOC 3) Used Gasoline RVP 7 properties for condensate loading emissions 4) See attachedTANKS 409d monthly runs for short term max vapor pressure values and annual runs for average vapor pressure
Table B-4 Maintenance Startup ampShutdown (MSS) Emissions 10 MSS Emissions from ScheduledRoutine amp Predictable Events Lindrith Compressor Station Enterprise Field Services LLC
Event DMcrlptlon Volume Per Event (MCF)
Events per h011r
Events per year
Hourly Volu~(~F
Annual Volume (~MCF
Material Vented
Standard ~cfllbmol Totallbmollhr -- middotmiddot J~llblo~r
Blowdowns 988 1 300 9 88 2 96 NalGas 379482 2804 781065
Planned maintenance and e shutdown 1375 1 15 1375 021 Nat Gas 379482 3623 54350
Compressor Engine Startup 161 1 512 161 082 Nat Gas 379482 423 216683
Total 399
Compound
DrymiddotBQII
M~le MW
lbflb~ lblhr tonaJyr
C02 0 4520 4401 020 tUl 105
N2 16971 2801 048 3U 2 2-SC)
Methane 752957 1604 1208 30331 en~middot
Ethane 11 6789 3007 351 wu ampQ
Propane 65968 4410 291 19345 1530
i-butane 08947 5812 052 3458 274
n-butane 18481 5812 107 7143 565
i-pentane 04973 7215 0 36 2386 189
n-pentane 04323 7215 031 2074 164
n-Hexane 0 1013 8618 009 581 046
Benzene 00133 7811 001 069 005
Toluene 00108 9214 001 066 0 05
Ethytbenzene 00006 10617 000 004 000
Xylenes 00035 10617 000 025 002 c6bull 04801 86117 041 2749 2 17
Total 10000 Avg Wo= 2197
VOCTotal
HAPTotl
37901 2998
745 1 059
1) See attached extended natural gas analysis dated March 9 2016
TANKS 40 Report
Identification User Identification City State Company Type of Tank Description
Tank Dimensions Shell Height (ft) Diameter (ft) Liquid Height (ft) Avgliquid Height (ft) Volume (gallons) Turnovers NetThnoughp~gaVyr) Is Tank Heated (yn)
Paint Characteristics Shell ColorShade Shell Condition Roof ColorShade Roof Condition
Roof Characteristics Type Height (ft) Slope (ftlfl) (Cone Roof)
Breather Vent Settings Vacuum Settings (psig) Pressure Settings (psig)
TANKS 409d Emissions Report - Summary Format
Tank lndentification and Physical Characteristics
Enterprise - Lindrith 450-bbl VFR Rio Ariba County New Mexico Enterprise Products Vertical FIXed Roof Tank 450 bbl Condensate (Gasoline RVP 7)
2000 1275 2000 800
1890000 1667
31506300 N
GrayMedium Good GrayMedium Good
Cone 000 006
000 000
Meterologicai Data used in Emissions Calculations Albuquerque New Mexico (Avg Atmospheric Pressure = 1215 psia)
summarydisplayhtm[l31201 7 32804 PM]
TANKS 40 Report
TANKS 409d
Emissions Report - Summary Format
Liquid Contents of Storage Tank
Enterprise - Undrith 450-bbl VFR - Vertical Ftxed Roof Tank Rio Arlba County New Mexico
Liquid Dolly Liquid Surf Bulk Vopor Liquid Vopolt
Tompondu (dog F) r VOIgtOI P_(peio) Mol Mooo M- Mol B-lgtr Vopor Puro
MbdllrwComponont Month A11 Min Max (dog F) Avg Min Max Weight Frad Frli Wolgllt CbullICJJidorw
Notul Gu Conclonoato (RVP 7) 878 53113 8079 5e23 5 20115 4 0811S 85018 500000 20700 124-Trimolhylbonlona 00273 00180 00451 1201900 00033 0 0001 12019 Opllon 2 Ao704383 Bz1573287 C=20856
Berw~ne 14274 0118411 20237 781100 00080 00008 7811 Option 2 A=BII05 8=1211033 C=220711
Elhylbonuno 0131Ml 00878 02182 1081700 00040 00004 10817 Option 2 Ameamp75 8=1424255 C=21321
Haxano(middotn) 23100 18303 32059 881700 00040 00078 8017 Option 2 Ame878 8=117117 C=22441
loooclano 07608 04C1211 11187 1142200 00010 00008 11422 Option 1 VP80 =58 VP70= 812 leopropyl benune 00870 00408 01072 1202000 00010 00001 12020 Option 2 Amell63 Sz14807113 C=20778
Toklono 04138 02720 08120 921300 00100 00033 9213 Opllon 2 A=BG54 8=13448 C=21948 Unldontllled Compononlo 58730 58439 55448 495789 09587 09801 21817
xytono (middotm) 01185 00728 01amp13 1081700 00140 00013 10817 Option 2 Abull70C8 8=1482280 C=21511
summarydispiayhtm[l3112017 32804 PM]
TANKS 40 Report
TANKS 409d
Emissions Report - Summary Format
Individual Tank Emission Totals
Emissions Report for Annual
Enterprise - Undrlth 450-bbl VFR- Vertical Fixed Roof Tank Rio Arlba County New Mexico
II Losses(lbs) I Components Worting Lossll Breathing LossJI Total Emissions
Benzene 99711 186811 28661
lsooctane 08711 16411 2511
Toluene 46211 90211 13841
Ethylbenzene o6sll 12211 1871
Unidentified Components 14363111 26904711 4126781
Natural Gas Condensate (RVP 7) 14654611 27451011 4210561
I Xylene(-m) 1ooJI 35611 5461
I Isopropyl benzene oo811 01511 0221
I 1 24-Trimethylbenzene 01011 02011 0301
I Hexane (-n) 107611 201611 30921
SUIII1Jia1)displayhtm[l3112017 32804 PM]
j ~~ -
Vmiddot1 01
7
Tomporolure _
tot Stege
7 VLV-101
I 311ee I 1 150ooJps~g
Sid ldul Uq Vol Flow I00000 I bamoVdoy
VLV-100
11
Temperature ~800 I F
PrassUTO 119121 polg
1 Molar fooW I 0501 I MMSCFD
13
Tampomtul ~aoo I F
Pr-re I 2l50o I pslg
Molar Row I esotl MMSCFD
Pigging lJqUid
Tomperoture 17500 IF
JgtfOOOIJra I~ooo Ipolg
S1d ldl Uq Vol Flow I7700 IbarreVdoy 1 5
~ 17 Sollntor
I 8k1v
Tore F
Pf01501J111 pslg
Molar flow MMSCFD 4
FlowtDS1Drllgo
MFiow
Tomporoblre p
Phuo middot Mus Flow(VOjiOUf Phuo)
_tgtHo Sid fdoalliq Vol Flow (Mixed 1lquld Phon
voc Vonlod
[ii48 JiblhrJ
4
TemPQnlturbull I38881 F
PreMUre 16ooo_l Plt~ Sid ldoollJqVal FlowI 1~0 I-middotY
n
r
Mlll-100
1888 lblhr
3438 F
00000 pslg
S248 lblhr
1836 b~
- middot itl l n bull 1
2G Tmiddot102i
~L l~ 24 ~
25 ~ L~
Thu Jul28 152642 2016 Case P Lindrith Compressor Station_Winter Case 3hsc Flowsheet Case (Main)
90
aspen ENTERPRISE PRODUCTS OPER Bedford MA USA
Case Name Lindrith CompressorStation_Wenter Case 3hsc
UnetSet NewUser1
DateTime Thu JuJ 28151052 2016
Fluid Packege Basis-1 7
8 Material Stream Flow to Storage
Property Package Pang-Robinson
10
CONDITIONS
11 Overall Vapour Phase Liquid Phase Aqueous Phase
12 Vapour I Phase Fraction 00517 00517 09109 00373
13 Temperature (Fl 3438 3438 3438 3438
14 P~ure (ps~) 00000 00000 00000 00000
15 Molar Flow (MMSCFD) 01701 8800e-003 01549 6352e-003
16 Mass Flow (lblhr) 1686 3248 1841 1258
17 Std Ideal Liq Vol Flow (barrelday) 1686 5076 1627 08821
18 Molar Enthalpy (Btullbmole) -8863e+004 -4197e+004 -8984amp+004 -1238e+005
19 Molar Entropy (Btullbmole-Fl 1816 4358 1699 1129
20 Heat Flow (Btulhr) -16556+006 -40566+004 -1529amp+006 -8838e+004
21 LJq Vol Flow Std Cond (barrelday) 1657 5904 1807 08478
PROPERTIES
24 Overall Vapour Phase Liquid Phase ~ueous Phase
M~IBpoundUJrVVelght _ __ _ 9_()_ 3362 ---~ _ 9645 ___ 1802
IVolarDenstty middot-shy middotmiddotshy middotmiddot (lbfO~elft3) ____ 41_95EtoO~ 2806~03 _____ 04603 ___ 3552 Mass Density (lbft3) ___ _ 1middot119 9432e-002 4439 __ __ 8398
28 Act Vol~me Flow (barrelday) 1631 1472 1580
~ Mass Enthalpy (Btullb) -S819 -1249 -9315
~ _Mass _Entropy ___ _ (BtuJ~middotF) middot----middot 02011 ----~--- 12~~- -middot _ ______ 01762
~ Heat Capacity __ (Btullbmole-F) 4267 - ---middot-middotmiddot-shy 13_68 ~ Mass Heat Cap_a_~_ty (BtuJibf)
~ LHV Molar Basis (s_td) __ (Etunbmole)
~ HHV Molar Basis (Std) (Btunbmole)
~ HHV Mass Basis (Sll) __ __ (Btullb)
~ ~2L~ _____ __
04727
173amp+006
18~7~06
2046e+004middot-
04070
6704e+005
7270e+005
2183e+004
4531
04698
1853amp+006
1986e+008
2059amp+004
4882amp-005
08395
-6874
- ---- 0~667 ~--- - --shy 1861
1033
1425e-004- 17636+004 -
9787
1804005~ C()2App~Con (l~retft3) ------middot ~ co2App_qon __ ClbiI~IY __ _______ _____ _ ___ _ _ ____ __ 11ooe-oo6 __ 28~~7
39 LHV Mass _la~s (Std) _ (~) 1909e+004 1994amp+004 1922amp+004 7909amp-006
~ Ph~seFracti_gtllJVCmiddotBasis] 3011iHgt02 middot---~ _ 30~~~02_ ____ 09648 - -middotshy - ~middot~103 ~ Phlse Fraction [~~~~s Basis) _ 1927e-002 1927e-002-~ Phase fra~lon_[~~Y~I Basis) ____ 09026 ______ 09026
~ -middot~~-EJlergy ____ (Btull_b)_ ___ ______ 1_9~ _______
09733
9688e-002 7~~~0~ 5147e-004
~ Partial Pressure of CO (pslg) _____ ~4middot6~
~ _9_ost Basecj on FIOV _ ____ (Costs) ------middot OcQ91)0 00000 _____ 00000 _______ 00000
~ -~~middot (3a_s flow (A9FM) ___ -shy-middot ~~ --- -- 5740 -------middotshypound Avg ~11 D11ns1ty _ (lbmo~~ --~- _ Q17_~~ 08137 04471 _______ 3458
~ SpeclficHeat _____ (Btullbm()le-F) _______ 427~7 1368 ----middotshy 4531 1861
Sll_ Gas Flow (MMS9~[)) 01698 8783e-003 01547
~ Std Ideal Llq_~a~lllnslty (~13 ----middot--- middot-middotmiddot 4275 ______ 2736 __________ 4312
8340003
6230
~ ~ct Llq FI()W middot middotshy----shy (U~GPM) -middotshy ___ 4_83~ 4609 ___ 24481_-QI)~ ~ ZFactor middotmiddot-middot----------middotshy ___ 09879 _ __ __ 6~~~~-003 middot _7_ 8056-()Q ~ Watson K _ __ ___ __ 1260 1593 1258
~ _serP~ertY _ _ __ _ _______ _
8510
~ - ~a(ti_aiP(9SSUf60fli2~ ---~ig_) ____ -1470
~ 9~(p_- RL_ _ ______ _______ ~04_~ middot-middot----- -~170_ ---middotmiddot-middot 1046 1119-------shy~ CpCv___ middot---shy __ __ ~middot09~ ______ 1178 __ ____ 1048 ----- ~~129
~ Heao~Vap middotmiddot---shy (Btunbm()~) _____ _961)e+004 -----middotmiddotmiddot
~ Kinerr1a~ Yi~o~tty (csectt)_ 5904 ____ middotshy _ _ 07928 _--middot----middot-shy _ 1 8~ ~ ~lq Mass D11nsity (5~9ld) Jlblft3) 4349 2352 ___ -~~ 8335
~ IJq V()l Flow (Std Cond) (b~lday) __ _ ~857 _ _
62 Llauld Fraction 09483 00000
5904 1607 08478--------middotmiddot -shy 1000 1000
63 Asoen Technoloav Inc Asaen HYSYS Version 88 (34008909 Pace 1 of5 Licensed to ENTERPRISE PRODUCTS OPER bull Specified by user
aspen middot bull1
ENTERPRISE PRODUCTS OPER
Bedford MA USA
Case Name
Unit Set
Daternme
Lindnth Compressor Station_Winter Case 3hsc
NewUser1
Thu Jul 28151052 2016
Material Stream Flow to Storage (continued) Fluid Package Basls-1
Property Package Pang-Robinson
2 10
PROPERTIES
11 Overall Vapour Phase Liouid Phase AQueous Phase
Molar Volume (fl3lbrnole)
(B_Lllb)~ -~a~Heat~fVae _
r Pha~~ Fract~l_l_MI_Ia_r aass _
1 Su~Tensk~ ___ _ _(d~n~tm)
) Thelal Clnducti~ty _ _Jtulh~-ft-F)
V~l_lty _ ___ middotmiddotmiddotshy ~P) 1 Cv (S~mildeal) (f~lbmole-F)
1 Mass Cv_(Sem_i-lde~l) __ (BtlJ1~)
~ Cv _____ (~MJbmo~e~F)
l Mass Cv __ (BulbR)
~ _Cv (E~ M~od) (B~_bmo~~F)
~ ~~ss Cv (irt Method (~tulbRJ ~ CpCv_(Ent t_lethod) _
~ __ Reidll~at3~C ____ __ (ps~g)
~ True VP at 37~c (psig)
~ _Uq VCf_ Flow- 5_Jm(Std ~~da_yen) 28 VIscosity Index
2D43
3211 _ _ _ _ 00517
_____ _
middotmiddotmiddotshy4069
04507
4256
04715
_ ________2148
_ _ middotmiddotmiddotshy middotshy ~706 1675
~6055
3564
00517
middot--shy _ 1159~lt1
- -middot ~middot~20amp-()0~ 11 70
03460
1161 middotmiddot--shy middot -------shy 03~~--
7239- ----------shybull _1_23 5904
2173
-shyQ910_
-shy- _ _21~--
7144amp-002 --05637 -shy---middot middotmiddotmiddotmiddot middotmiddotmiddotmiddotmiddot
4332
04492
---shy- - 4332 04492 --shy -shy--middot--middotmiddotmiddotmiddotmiddot
4190
1482
1607
02816
1----shy 00373
______ 7617
03300 - ----shymiddotmiddotmiddot middotmiddotmiddotshy 1681middotmiddot---shy --- -middot 1662
09226
_ 16~
09147
_ 15 ~
08764_
1176
middotmiddot---~- -3 5~ -1~-50
01478
~ 30
COMPOSITION
Overall Phase Vapour Fraction 00517
COMPONENTS MOLAR FLOW
(lbmolehr)
MOLE FRACTION MASS FLOW
lblhr)
MASS FRACTION LIQUID VOLUME
FLOW (barreVday)
L IQUID VOLUME
FRACTION
~ CQ~ -shy- - ---middot ~H2S
~ ~~~~en -------middot ~ Oxy(lampl_l
~ Methane
40 Ethane Propane --middotmiddot-shy -shy
_ __ 009Q_O
000~ __ ___ QOOOO_
03900
-----shy 0 _4154
middotmiddotshy - --shy-shy Q9795
~ ~~Uialf ---middotmiddot-shy middot-middot middot-shymiddot-middot _Q~_788 2 J~Utal --------shy middot--~- _1_~~ _ ~~n~ne 08590
~ nfgten~~L - -middot---middot 1_QQ1
2 C)CIOp911~~ _ __ ~bullQ~ ~ n-Hexane ______ __ ___ __ )7l~t
~ CycJ~hexane __ __ _ ______03987
~ _l1~~ne 22957
~ -~cyclohexanl_l ___ _____ _ - middot--shy _ _ Q_9336
~ ~~~~~ntan~- __ ~-==~ ~~~ ~ Toluene 03179
~ E~enzer1~ 00461
~ p-~ylen~ ---middot----- _ middotshy--- ---shy 02950 ~ n-O_~ne ___ __ _ ----~- 22371
~ H20 ---shy middot _ ___Q706Q_
~ n-Nonane ___ _ middotmiddot-shy___ 94~1
59 n-Decane 27947
00004-----middot 00000
00001 - shy -shy middotmiddotmiddotmiddotmiddotmiddot ____ _ QQQOO
00209
- --middotmiddot QO~ 00524
00203 middot --~------
___ _ _()062Q
00460
00557- ------middot-shymiddot-- shy -shy00048 ----middot middotshy---shy --shy01491------shy -middot-- middotshy
----- - 00213
01229
00500
00001
00063 ---shy-- --middot--shy - - -middot
00170
00025
00158
01198
00378 shy-shy middot--shy ~---
00230
01496
03113- - - - -middotmiddot 00000
00647
middotmiddotmiddot--middotmiddotshy-- QOO~ 1 62572
124903
431918
~-Q181
_ 87 ~~75
61 11_7~2
750420
62241
2399238 - -middot---shy33~
2300423
916710
01716
92534
292874
48969
313206
2555483--shy ---- middotmiddot middot-middot 127183 middotmiddot middot - -shy550392
3976499
---shy
- ----shy
00002
00000
00000
99000
00037
00074
00256
00131
--shy 00399
00388
- --shy 00445
00037
------shy 01423 00199
--shy-shy middot
01364
00544
00001
00055
00174
00029
00186--shy --shy middot middotmiddot-- middot- middotmiddotmiddot
01516- -shy - ---shy
-shy -middotshy -
00075
00326
02359
-middot - -shy
58370
26828
79045
66068
- -----middot ~15)~ ----- Q5691
- -- 2_1 791~ 2_9~~
229343
81263
00169
07182 ~ -- -
23049
03854
24815-shy- ----shymiddot 248068---- --shy --shy - middotshy
08726
52325
371604
-- ----shymiddot-shy
00002
()0000
00000
Q_O()OO 00085
00143
00346
00159
middot--shy 00469 00404
--shy--shy 00484
- --shy - QOO~~ 01470
---shy 00174
01360-- --middot-middot middotshy ---- shy
00043
00137
00023
00147
01471-------shy --shy -00052
00310
02204
60 Total 188772 10000 18859812 10000 1885966 10000
~ 62
63 Asoen Technoloav Inc Asoen HYSYS Version 88 (34008909 bull Paae 2of5 Ucensed to ENTERPRISE PRODUCTS OPER bull Specified by user
Case Name Lindrith Compressor Stat1on_Winter Case 3hsc
aspen ENTERPRISE PRODUCTS OPER Bedford MA Unit Set NewUser1 USA
DateTimemiddot Thu Jul28 151052 2016
Material Stream Flow to Storage (continued) Fluid Package
Property Package
Basis-1
Pang-Robinson
COMPOSITION
~ 12 Vapour Phase Phase Fraction 5173e-002
~ COMPONENTS 14
MOLAR FLOW (lbmolehr)
MOLE FRACTION MASS FLOW (lblhr)
MASS FRACTION LIQUID VOLUME FLOW (barreVday)
LIQUID VOLUME FRACTION
~ Y9~ -------shy -shy- 00053 00054 02317middot-shy -shy middotmiddotshy ---shy 00071 --~ - --middot ----=00192 00038-shy-shy ----shy -
~H2S 00000 ---- 00000 -shy--middot 00~_00 00000------ --shy OOOQQ -shy--middot ()()000 N_ibPg~n ___ __ _____ 00022 -shy~ _QQO~ - - - 0063Q (_10()~_9 00053 00011---shy - _18 ()J_ltYllen 00000 00000 00011 00000 00001 - - - middot- bull
00000 19 Methane middot--shy------middotmiddot-shymiddotmiddotshy --middot-middot-middotshy 03521 03644 middot--shymiddotshy middot-middotmiddot-middot 56485 ---shy - - -shy -shy -- -shy 01739 12918 02545--shy- middotmiddot-middot middotmiddotmiddotmiddot-middotmiddotmiddotmiddotshy -shy - ------shy---shy -------~
a fsectth_lne middotshy-----~ _ ____ g2~9 69418 02137 13364 --shy-shy 02633
~~ middot----shy 02160 95235 __----middotmiddot Cl~l -~ __ _t_28P ________ o2~ 22 i-8utane
middot----middot--middotmiddotmiddotmiddotmiddotmiddot - ----shy 00328 -~~
00340 ___ _ 1907_~ middotmiddotmiddotshy-shy 00587 - -- ()232~ ______QQ45~ ~ = n-Butana 00687 00711 39943 01230 04689 0(_1924
~ i-Pentane 00183 00189 1-~~1 00406 01450 - 00286
~ ~t~ne - ---shy~shy --~-shy-gt9157 -----shy 00162 11313-shy- -----shy 00348 1 1__239__ 00242-------shy~ CyiI9P_l_nlllne ____ --middot - - 00010 00010 00681 00021 00002 00012- -----shyZT r- n-la~-n~- _ __ __ OD108 - 0011~ 0_~292 00286-------- shy 00960 00189
~ Cyclohexane 00~12 00013 01018 00031 00089 00018
~ n-Heptan~ 00024 00025 02391 00074 00238 00047
~ flllcyc_lohexana O()Q12 middotshymiddotmiddotmiddotmiddot middot -~ --shy 0001~ 01144- -----middotshy ~ -- -----shy 0(_1035 00101 00020
~ ~241-Ape~lan~ 00000 - shy -- shy--middot 00000 00000 ~0000 00000
Benzene------shy -middot 00004 QJ095 00011 - ---shy middotmiddotmiddot-shy 00027 00005
~ Tol_uene 0~~ Oc0003 00009 00022 00004
~ E-~11nzene 00000 ooooo 00000 00001 00000
~ Jl~)_(yten_~ _______ 00001-middot-middot--middot - -----shy 00001 00002 00005 00001
~ n-Octane _ ____ _ 00006------shy --- middotmiddot- 00008 00716----shy ---shy - -------shy 00022 00070---shy ---shy -- 00014- ---shy --shy
~ H20 - - shy - )(_1062 00064 -middot --shy - 01121 00035 00077 - --shy 000015
~ 1-lio_nafll _ _ _ _ ___ _gt~~0 shy -shy 9QOQltgt 00044--shy -----shy _ ___00001 _ _ ___ OQQ(l4 - --- 0()_0(1 39 n-Decane 00001 00001 00094 00003 00009 00002
40 Total 09663 10000 324832 10000 50758 10000
Liquid Phase Phase Fraction 09109
r2 COMPONENTS 44
MOLAR FLOW (lbmolelhr)
MOLE FRACTION MASS FLOW (lblhr)
MASS FRACTION LIQUID VOLUME FLOW (barreVday)
LIQUID VOLUME FRACTION
~ _CO~ ----~-shy
~ fl_~s middotmiddot- shy ----shy~ ~~gen __middotshy ---middotmiddot
~ Q~~n ~ MIIJane ~ l_~ne
_middot--shy _ __ _
i-B~ne _ ___ -middot-middot
n-BIJUina _ ~ 1-Pentan_e
~ n-Pentane middot- ---shy~ Cyclo~_~l1-~ _ ____
n~fiexane _ _~-shy _ Cyc~ohexane _ _
~ ~tfEIPIIIne _Mc_y~ohexane ___ _
24-1~ne - -shy -62 Benzene
~I ProJlltln
2
2 2_
2 1
middotmiddot-middotmiddotshy - middot OOO~IS middot--shy ooo~(_l_
00001
-shy - - (_1 0~0 00379
()1~5
0~5 03480
10896
08407
10244
00878----------shy -shy27733
03975
22933
09325
00015
01180
0-()~1
middotmiddotshy - - OOO(_IQ
middotmiddot--shy--middot-shy (_10000 ooooo
- shy _00_022 0(_1108
OO~J 00203
008~0
00494
00602
00052 -----shy- shymiddotmiddotmiddotmiddotmiddot 01630
00234
01348
00548 00001
00069
- - - 00794 00000 -shy -- -middotmiddotmiddotmiddotmiddotmiddotmiddotmiddotmiddot
- shy---shy 00017
(J()OQ1
06087
55484
336684
201105 middotmiddotmiddot-middot----middotmiddotmiddot 633332
~-6541
739107 middot -~- ----shy
61559
2389948
~4544_ 2298032
~~5~~ -shy01714
92188
00000
00000- ---shy -middot -middotmiddot----shy00000
00000
00004
1gt0034 00205---shy - 00123
00386
00370
00450
00036- -middotmiddot middotmiddotmiddot -- ----shy01456
--middotshy~ Q()204 01400
00558
00001
00056
00066
OQ()OQ
00001
00000
01392
10681
45500
24504
74356
66617
80366
-middot-- middot- 0_~2~ 246952
2-90_() 229105
81162
00169
07155
00000 -middot-------shy
00000- -----shy
-------middotshy
00000
00000
00009
00066
00280
00151
00457
00410
00494
00035
01518
00180
01409
00499middotshy middotmiddot - - -00001
00044
63 Asoen Technoloav Inc Asoen HYSYS Version 88 (34008909 Paae3of5 Ucensed to ENTERPRISE PRODUCTS OPER bull Specified by user
Case Namemiddot Lmdnth Compressor Station_Winter Case 3hsc
aspen middot middot~
ENTERPRISE PRODUCTS OPER Bedford MA Unit Set NewUser1 USA
DataTimemiddot Thu Jul28 151052 2016
Basls-1Fluid Package
Property Package Material Stream Flow to Storage (continued)
Peng-Rob1nson
~ 10
~ 12
~ COMPONENTS MOLAR FLOW 14 lbmolelhr)
To)ue~~ __ __ __ _ _ _ _ 03176
E-Be~ne ---middot--shy middot-middot-middot- shy 00461 p-_)(~IBIl -----shy - middot_ __ 02950
~ n-(c_llne _ middot middot- middot shy - 22365 H20 ____ -middot 00023
~ n-N~nne ___ _ _ ---shymiddot 04291
21 n-Decane
22 Total
~ 24
~ 26
~ J ~ ~ ~ ~ shy~ ~ ~ ~ ~ ~ ~ ~ 41
~ ~
COMPONENTS
C02 H2S
JIIitrtl~n -middot OClJ_Bn ----middot ___ M~thane
Ethane
Propane 1-B-_Jian(l n-Butane
1-P~-~n~
~l~ne _
CYciOP~a- ---shyn-Hexane
Cycloh~~shy~ ___ _
n~Heptan~
McyclohBllfll____
2 ~4-Mpe~tane __ _ ~ Benzene
45 Toluene
27947
170135
MOLAR FLOW (lbmolelhr)
00000
00000
00000
00000
---middot middotmiddotQ-0000 00000
----shy
00000
00000
00000
00000
00000
00000
00000
00000-- middot-- --shy -middot 00000
00000
00000
00000
00000
COMPOSITION
Liquid Phase (continued) Phase Fraction 09109
MOLE FRACTION
00187 -----middotmiddotmiddotmiddotmiddotmiddotmiddot ----shy middot 0 ~0~7
00173
01315
00001
00252
01643
10000
MASS FLOW (lblhr)
292598
middot- -middotmiddotshy -~~~57 - -middot-shy _3_q~
2554767
00414
550348-shy -----middot
3976405
16409331
MASS FRACTION LIQUID VOLUME LIQUID VOLUME FLOW barrelday) FRACTION
00178-- --middot 00030 - --middot -middotmiddot-middot
-shy --- -shymiddot 23028 03853
- ---shy - 0lt_19~-shy - -middot- 248~Q 01557 247998
00000 00028
--shy oo_~ 02423
10000
middot-shy52321
371595
1626587
00142-- ------shymiddotmiddotmiddot---middot-shy-middot 00024
- --shy- --middot
00153
01525
00000
00322
02285
10000
Aqueous Phase Phase Fraction 3734e~02
MOLE FRACTION
00000
00000
00000
00000
00000
00000
OQOQQ
00000
00000
00000
00000
middot--shy 00000 00000
MASS FLOW MASS FRACTION (lbJhr)
00002 00000-----shy00000 00000
00000 00000
00000
00000
00000
00000
00000
00000--shy ------shy00000
00000
_OOOOQ 00000
00000
00000
00000
00000----shy -shy - -shy
00000 --middot - - - 0shyQQOO
LIQUID VOLUME FLOW (barrelday)
00000
00000
00000
00000 00000
00000
00000
00000
00000
___ poooo 00000
00000--shy middot 00000 middot-shy--- Q_~ 00000 0~0- 00000
00000 00000 00000 - - middot -shy ~0_00) oqooo 00000
00000
00000
00000---shy -00000-------shy
-middot----- Q()()()O _ middot--middot C~OOO
00000 ---- 00000
00000 middot-----shy _O Q~~ 00000 -shymiddotmiddot--shy 00000 00000 00000
LIQUID VOLUME FRACTION
00000
00000
00000
00000
00000
00000
00000
00000
00000
00000
00000
OOQl9 00000
000~
00000
00000
- -middot---shy 00000 00000
00000 --middotmiddot---shy OQOO( _ _ __ _()QOOQ ----- 00000 - - --middot-middotmiddotmiddot 00000fa E-Benzene middot-shy --shy -middotmiddotmiddotmiddotmiddotmiddotmiddotmiddotmiddot-middot-middotmiddotmiddotmiddotmiddotmiddotmiddotmiddotshy - - 00000 middot---middot 00000 ____ 00000 middot--shy- O_q()()Q_ _____ QOOOO 00000
~ p-Xyene _ --middot
~ n-O~nl -middot--shy2 H20 _ n-Nonane
51 n-Decane
52 Total
00000 --shy-----shy -00000-- ---shy -shy middotshy
06975
00000
00000
06975
COMPONENTS
~ - -shy -----shymiddot----middot--~-- C02 ~ -middot middotmiddot - _ - - shy - -shy -middot H2S
~ ~ ~ ~ 62
__ _ Nitrogen
_()xygen Methane ------middotmiddotmiddotmiddotmiddotmiddotmiddotmiddotmiddotmiddot -middot
- shy middot--middot-middotshy - ---shy - -middot--middotshy ___ Ethane Propane
63 Asoen Technoloav Inc
00000 00000 middot-middotmiddotshy00000
00000
10000
00000
00000 00000 00000
00000
00000
10000
00000
00000
- --shy middotmiddotmiddot-shy --- 08621
00000---middot----shy
125648
00000
00000
10000
00000
00000 - - --shy-shy
00000
10000 125649 10000
KVALUE
MIXED LIGHT
middot-----shy ----shy 5338 middot------shy--shy ---~1 38
-----shy---shy - - ~0-5_ 2749- - -shy middotshy middot-------- ----- bull
1701 2293
- - ------- -shy --middotmiddot
6541
2641
1634
--middot-middot-shy --shy 2203 5185 4981
Asoen HYSYS Vers1on 88 (34008909
00000
08621 10000
HEAVY 1073- ---shy- - shy-----shy
4796e-+)04
5985e+005
8934e+008 middotmiddotmiddotmiddotshy ---- middot---- ----middotshy - - ----shy
middotmiddot-- - -shy- ----- 8494e+010 2835e+013
Paae4of5 Ucensed to ENTERPRISE PRODUCTS OPER bull Specified by user
Case Namemiddot Lindrith Compressor Stat1on_W1nter Case 3hsc
aspen middot1
ENTERPRISE PRODUCTS OPER Bedford MA USA
Unit Set NewUser1
DatefTime Thu Jul 28 151052 2016
1 8
Material Stream Flow to Storage (continued) Fluid Package Basis-1
Property Package Peng-Rob1nson
10
KVALUE
11 COMPONENTS MIXED LIGHT HEAVY
E 1-Butane 1739 1670 bull _ -~-492e+(l1_f
~ n-Butane 1156 1J1~ 1898e+016 middotmiddotmiddot---- -middotmiddot
~ _ ___ ________ iPentane 03989 --------shy 03832 3467e+019--shy - -shy --shy -- - shy -~ - --shy- - - ___ i_PampIlta18 middot -----shy - 02806 --------shy 02695 2858e+019----shy-shy -shy~ ------middotshy ________C_rclopnla~~ 02029 01949 middot--shy-shy- -shy02~15 ~ - --------shy--shy ____ _r~Hexan~ _ _ ______ _1_6e-OQ __ ___ _____ ~846e-002 7119amp+022 --------middot -----middot-middot middotmiddot
~ Cyclohexsne 5578e-002----shy 5359amp-002 68148+017 middotmiddotmiddot-shy
~ _ n-He~~~ - 1907e-002 1632e-002----------shy- -------------middot bull - 3108amp+026
~ - - - shy - ----shy --~C)pound)ghexa~ 2290amp002middot--shy---shy - - - shy --middot 2200amp002- ---- shymiddotshy - shy - -- _______ 4~11e+(l~1
~ 22~MI)8flla ---shy ---shy ~_09~~ 2026e-002 -~ ~----- -shy
~ --shy------shy-------shy _B~~e middotmiddotmiddotmiddot------middot-----~~16amp-00 6614e-002-------shy ------shy - -----shy4709e+014--shy -------middot-shy -middotmiddotmiddotmiddotmiddot -shy middot---shy -shy
~ Toluene 1-~e-001 1864e-002 2036e+018-
~ E-Bel)zene 4553e-003 4373amp003 33548+021
~ ____ --------------~Xylene 3788e-003--- -----shy --------shy--shy ---shy-shy- 31~e-003 ~13a+022
~ _____ --shy middot- middot ~ne 5139e-003 4936e-003
~ H20 01630 - - --shy 4772 64426-003
~ n-Nonane 1459amp003 1402e-003
29 n-Oecane 43448-004 4173e-004
63 Asoen Technoloav Inc Ascen HYSYS Version 88 (34008909 Paoe 5of5 Ucensed to ENTERPRISE PRODUCTS OPER bull Specified by user
Meter Number Meter Name Location Sample Date File name
Component
Inlet Gas Analysis
SJ Lindrith lnlet3-9-16 Lindrith CS 392016 SJ LINDRITH INLET 3-9-16_1 0
Mol Wt
Flow Pressure 51 Flow Temp 49
H20 LbMMCF shyH25 ppmmol shy
Type Spot Pulled by Blaine Ellis
LV Carbon Dioxide Hydrogen Sulfide Nitrogen Oxygen Methane Ethane Propane I so butane n-Butane lsopentane n-Pentane Cyclopentane n-Hexane Cyclohexane Other Hexanes Heptanes Methylcyclohexane 224 Trimethylpentane Benzene Toluene Ethylbenzene Xylenes C8+ Heavies
Total
04520 00000 16971 00110
752957 116789 65968 08947 18481 04973 04323 00272 01013 00388 02320 00876 00455 00000 00133 00108 00006 00035 00356
1000000
09050 00000 21630 00160
549594 159780 132352 23660 48872 16325 14189 00867 03973 01487 09040 03972 02031 00000 00472 00451 00028 00170 01897
1000000
03971 00000 09612 00050
657186 160803 93568 15073 29996 09363 08067 00414 02145 00680 04737 02022 00940 00000 00191 00185 00012 00070 00913
1000000
Houston Laboratories 8820 Interchange Drive Certificate of Analysis
Houston TX 77054 Number 1030-15080180-001A Phone 713-660-0901
Gary Turner Aug 112015 Enterprise Products 614 Reilly Ave Farmington NM 87401
Station NameLindrith Compressor Sampled By GT Sample Point Pigging Liquids into Plant Sample Of Liquid Spot Cylinder No 8963 Sample Date 07282015 11 45 Analyzed 08062015171520 Sample Conditions 50 pslg 75 bullF
Method GPA 2103M
Analytical Data
Components Mol MW Wt Sp Gravity LV
Nitrogen 0012 28013 0002 0807 0002 Methane 1524 16043 0149 0300 0400 Carbon Dioxide 0026 44010 0007 0817 0007 Ethane 1823 30069 0334 0356 0755 Propane 3989 4409() 1072 0507 1703 I so-Butane 1253 58122 0444 0563 0635 n-Butane 4181 58122 1481 0584 2043 I so-Pentane 2625 72149 1154 0625 1487 n-Pentane 3116 72149 1370 0631 1750 i-Hexanes 1718 85084 0891 0668 1075 n-Hexane 2422 86175 1272 0664 1544 224-Trimethylpentane 0070 114231 0049 0697 0057 Benzene 0464 78114 0221 0885 0201 Heptanes 11984 94444 6897 0722 7692 Toluene 1991 92141 1118 0872 1033 Octanes 12970 107994 8537 0740 9293 Ethyl benzene 0351 106167 0227 0872 0210 Xylenes 2241 106167 1450 0872 1341 Nonanes 6842 125606 5240 0749 5634 Decanes Plus 40398 276586 68085 0869 63138
100000 100000 100000
Physical Properties Total C10+ Specific Gravity at 60F 08058 08689 API Gravity at 60bullF 44110 31350 Molecular Weight 164088 276586 Pounds per Gallon (in Vacuum) 6718 7244 Pounds per Gallon (in Air) 6710 7236 Cu Ft Vapor per Gallon 14696 psia 15536 9939
Hydrocarbon laboratory Manager
Quality Assurance The above analyses are performed in accordance with ASTM UOP GPA guidelines for quality assurance unless otherwise stated
Page 1 of2
Gary Turner Enterprise Products 614 Reilly Ave Farmington NM 87401
Station Name Lindrith Compre~or Sample Point Pigging Liquids into Plant Cylinder No 8963
Certificate of Analysis Number 1030-15080180-001A
Aug 11 2015
Sampled By GT Sample Of Liquid Spot Sample Date 072820151145 Sample Conditions 50 psig 75 F
Analytical Data
Houston Laboratories 8820 Interchange Drive
Houston TX 77054 Phone 713-660-0901
Detection Lab Analysis Test Method Result Units Limit Tech Date
Shrinkage Factor Proprietary 09715 JB 08072015 Flash Factor Proprietary 357893 CuFtSTBbl JB 08072015 Color Visual Proprietary Crude JB 08072015 API Gravity 60deg F ASTM D-4052 4046 LC 08102015
Hydrocarbon laboratory Manager
Quality Assurance The above analyses are performed in accordance with ASTM UOP GPA guidelines for quality assurance unless otherwise stated
Page 2 of2
- Structure Bookmarks
-
- Figure
- ENTERPRISE PRODUCTS PARTNERS LP ENTERPRISE PRODUCTS OPERATING LLC ENTERPRISE PRODUCTS HOLDINGS LLC
- Enterprise
-
- Enterprise
- (General Partner)
-
- Products
-
- Products
- March 8 2017
- 7015 1520 0002 7267 0373 Return Receipt Requested
- Federal Minor NSR Permit Coordinator
- US EPA Region 6 1445 Ross Ave Suite 1200 Dallas TX 75202
- Re Enterprise Field Services LLC Lindrith Compressor Station Lindrith Rio Arriba County New Mexico Minor Modification of Permit Number R6NM-03-Rl
- Dear Sir ofMadam
- Enterprise Field Services LLC (Enterprise) is submitting this application for a minor permit modification to Permit Number R6NM-03-R1 which was issued on November 4 2015 AIR EMISSIONS IMPACT The change proposed in this application involves increasing the following limits within the CUITent air
- permit
- Page Current Limit Proposed Limit TBATTERY 3 3739 tonsyear 10263 tonsyear TLOADING 3 223 tonsyear 498 tonsyear MSS 3 2500 tonsyear 3000 tonsyear Condensate 7 20000 barrelsyear 60000 barrelsyear
- Throughput The increase of emissions is explained in detail in the attached calculation spreadsheets The activities
- which generate these VOC emissions are the storage of condensate and loading of trucks to remove the condensate to off-site destinations REGULATIONS IMPACT This application has been prepared in accordance with EPA guidance The current permit page 18
- paragraph 59 lists the limitations ofthe minor modification procedure as follows
- 5911 Do not violate any applicable requirement This application does not
-
- 5911 Do not violate any applicable requirement This application does not
- 5912 Do not involve significant changes to existing monitoring reporting or recordkeeping requirements in the permit This application does not
- 1100 LOUISIANA STREET
- P 0 BOX 4324
- HOUSTON TX 77002-5227
- HOUSTON TX 77210-4324
- wwltgt~enterpri6e)roductscom
-
- wwltgt~enterpri6e)roductscom
-
- 713381 6500
- US EPA Region 6 Lindrith Compressor Station March 8 2017 Page2
- 5913
-
- 5913
-
- 5913
- Do not require or change a case-by--case determination of an emission limitation or standard or a source-specific determination for temporary sources of ambient impacts or visibility or increment analysis This application does not
-
- 5914
-
- 5914
- Do not seek to establish or change a permit term or condition for which there is no corresponding underlying applicable requirement to which the source would otherwise be subject This application does not
-
- If you should have questions or need additional infonnation regarding this application please contact Robert Havalda at 713-381-6698 or by or Brad Cooley at 713-381-5828
-
- email at nnhavaldaeprodcom
-
- Sincerely
- Robert Havalda Bradley Coole Senior Environmental Engineer Senior Mana er Environmental Permitting
- bjm
- Attachments EPA Administrative Permit Amendment Request (Form AMEND)
- Process Flow Diagram
- Detailed Emission Calculations
- HYSYS Flash Analysis TANKS 409d Output
- Site Gas Analysis
- cc Mr Jim Lieb -Enterprise Products Operating
- Tribal Environmental Contact-Jicarilla Apache Attn Ms Bonnie Braganza P E
- US EPA Region 6 1445 Ross Ave Suite 1200 Dallas TX 75202
- Mr Cordell Tecube Environmental Protection Office Jicarilla Apache Tribe
- PO Box507 Dulce New Mexico 87528
- Enterprise Field Services LLC Lindrith Compressor Station Rio Arriba County New Mexico
-
- Minor Permit Modification Permit No R6NM-03-Rl
-
- Minor Permit Modification Permit No R6NM-03-Rl
- MARCH2017
-
- MARCH2017
- OMB Control Number Pending middot
- UNITED STATES ENVIRONMENTAL PROTECTION AGENCY FEDERAL MINOR NEW SOURCE REVIEW PROGRAM IN INDIAN COUNTRY Administrative Permit Amendment Request (Form AMEND)
-
- UNITED STATES ENVIRONMENTAL PROTECTION AGENCY FEDERAL MINOR NEW SOURCE REVIEW PROGRAM IN INDIAN COUNTRY Administrative Permit Amendment Request (Form AMEND)
-
- UNITED STATES ENVIRONMENTAL PROTECTION AGENCY FEDERAL MINOR NEW SOURCE REVIEW PROGRAM IN INDIAN COUNTRY Administrative Permit Amendment Request (Form AMEND)
-
- Please check box to show how you are using this form 0 Correction to a Typographical Error 0 Incorporation of More Frequent Monitoring or Reporting 11 Increase in Allowable Emissions (SEE INSTRUCTIONS) 0 Other
-
- Please check box to show how you are using this form 0 Correction to a Typographical Error 0 Incorporation of More Frequent Monitoring or Reporting 11 Increase in Allowable Emissions (SEE INSTRUCTIONS) 0 Other
-
- Use of this information request form is voluntary and not yet approved by the Office ofManagement and Budget The following is a check list ofthe type ofinformation that Region 6 will use to process information on your proposed project While submittal ofthis form is not required it does offer details on the information we will use to complete your requested approval and providing the information requested may help expedite the process Use ofapplication forms for this program is currently under Office ofMa
-
- Use of this information request form is voluntary and not yet approved by the Office ofManagement and Budget The following is a check list ofthe type ofinformation that Region 6 will use to process information on your proposed project While submittal ofthis form is not required it does offer details on the information we will use to complete your requested approval and providing the information requested may help expedite the process Use ofapplication forms for this program is currently under Office ofMa
-
- Please submit information to following two entities
- Federal Minor NSR Permit Coordinator
- US EPA Region 6 1445 Ross Ave suite 1200 6MM-AP Dallas TX 75202
-
- R6airpermitscmagov
-
- For more information visit shypermittinglcaa-permitting-epasshysouth-central-region
-
- httpwww2epagovcaa
-
- A COMPANY INFORMATION
- The Tribal Environmental Contact for the specific reservation
- Ifyou need assistance in identifying the appropriate Tribal Environmental Contact and address please contact
- R6airpermitsepagov
-
- R6airpermitsepagov
-
- Company Name (Who owns this facility) Enterprise Field Services LLC
-
- Company Name (Who owns this facility) Enterprise Field Services LLC
-
- Company Name (Who owns this facility) Enterprise Field Services LLC
-
- Company Contact (Who is the primary contact at the company that owns this facility) Robert Havalda
-
- Company Contact (Who is the primary contact at the company that owns this facility) Robert Havalda
- Title Sr Environmental Engineer
-
- Mailing Address PO Box 4324 Houston TX 77210-4324
-
- Mailing Address PO Box 4324 Houston TX 77210-4324
-
- Email Address nnhavalda~rodcom
-
- Email Address nnhavalda~rodcom
-
- Telephone Number Facsimile Number 713-381-6698 1713-381-6811
-
- Telephone Number Facsimile Number 713-381-6698 1713-381-6811
-
- B FACILITY INFORMATION
- Facility Name on the Permit to Be Amended Lindrith Compressor Station
-
- Facility Name on the Permit to Be Amended Lindrith Compressor Station
-
- Facility Name on the Permit to Be Amended Lindrith Compressor Station
-
- Minor Source Permit To Construct Number Not Applicable
-
- Minor Source Permit To Construct Number Not Applicable
-
- Date ofMost Recent Permit Action (this should be the same permit to which you are requesting the amendment) November 4 2015 (Permit Number R6NM-03-R1)
-
- Date ofMost Recent Permit Action (this should be the same permit to which you are requesting the amendment) November 4 2015 (Permit Number R6NM-03-R1)
-
- C DESCRIPTION OF THE PROPOSED AMENDMENT
- Provide a nanative description ofthe requested amendment to the permit and the following
- 1 Why the proposed change can be made through this form (See instructions)
- Enterprise Field Services LLC (Enterprise) is proposing to increase the allowable emission rate for
- the following emissions units
- 1
-
- 1
-
- 1
- Increase the annual throughput for condensate tank battery (Unit ID mATfERY) from 20000 barrels per year (bbllyr) to 60000 bblsyr (fBATIERY consists ofeight 454-bbl fixed roofstorage tanks)
-
- 2
-
- 2
- Increase truckloading (Unit ID TLOAD) emissions from 20000 to 60000 bbllyr to accommodate the increased throughput from TBATTERY and
-
- 3
-
- 3
- middot Increase Maintenance Startup and Shutdown (Unit ID MSS) emissions to accommodate the increase in the natural gas VOC content
-
- The proposed change in gas composition will add 7298 TPY of VOCs to the facility This facility is currently and will remain a minor NSR source
- 2 Information presented in enough detail to document how the facility is currently operating and how it is proposed to operate A narrative description ofall ofthe facility processes along with a process flow diagram to enable EPA to understand the effect the proposed change has on emission unit or (pollutant generating activity)
- The Lindrith Compressor Station is a natural gas compression and transmission facility that relteives naturalgas from a gathering system and compresses thatgas for transmission via pipeline The emissions units at the facility consists ofthree reciprocating ioternal combustion engines (RICE) that drive tbe compression units (Unit IDs A-01 A-02 and A-03) the emergency RICE generator (Unit ID EMERGEN) emissions from engine starts compressor blowdowns vessel and piping blowdowns and pipeline pigging ac
- Page2 of6
- 3 Emissions calculations and all supporting data necessary to establish the proposed post-change allowable emission limits The requested information must be provided for each emissions unit (or pollutantshygenerating activity)
- Attachment 2 contains emissions calculations tables and supporting documentation for each change requested
- 4 The proposed changes to be made to specific terms and conditions ofthe permit A redlinelstrike out version ofthe permit may be used for this purpose Enterprise is proposing the following changes to the specific terms and conditions ofthe permit Page Current Limit Proposed Limit TBATTERY 3 3739 tonsyear 10263 tonsyear TLOADING 3 223 tonsyear 498 tonsyear
- MSS 3 2500 tonsyear 3000 tonsyear Condensate 7 20000 barrelsyear 60000 barrelsyear Throughput
- 5
-
- 5
-
- 5
- The fillo owmg a ewt ac 1 y-wt e tnlSSlOll 1ma est bl th F irt d E Esf t
-
- TR
-
- Pollutant
- Pre-Change AUowable
- Post Ch~geAllowable
-
- TR
-
- Emissions (tpy)
- Emissions (tpy)
-
- TR
-
- PM PMto PM2s so2 NOs co voc Pb Fluorides H2S04 H2S TRS
- 291 291 291 426 6629 10257 13836 0 NA NA NA NA
- 291 291 291 426 6629 10257 21134 0 NA NA NA NA
- PM -Particulate Matter PM10 -Particulate Matter less than 1 0 microns in size PM2s -Particulate Matter less than 25 microns in size S~-Sulfur Oxides NOx -Nitrogen Oxides CO -Carbon Monoxide VOC -Volatile Organic Compound Ph -Lead and lead compounds Fluorides -Gaseous and particulates H2S04 -Sulfuric Acid Mist H2S -Hydrogen Sulfide TRS -Total Reduced Sulfur RSC -Reduced Sulfur Compounds
-
- TR
-
- RSC
- NA
- NA
-
- Page3 of6
- COMPRESSED NATURAL GAS TO PIPELINE
- EPHA-()1
-
- GASCOQER
-
- EPHA-02 GAS TO COMPRESSION
- ------------EPNA-03
- CATERPILLAR 36121pound 2ND STAGE GAS
- bull bull INLET SAPERATOR COMPRESSORS
- INLET GAS CONOENSAlE bull I
-
- INLET GAS CONOENSAlE bull I
- SWG CATCHER
-
- EPNFUGOC I bull UQUDS FROM INTERSTAGE EPNMSS
- COOLERSSCRUBBERS
- PIPING EPN BATIERY
- COMPONENTS
- NA~AL GAS FROM bull I tISS EVENTS
- STA110N BLOYlaquolOWN VENT
-
- I
-
- I
-
- 88881
-
- CONDENSAlE 1RUCK LOADING
-
- eeeer-H
-
- eeeer-H
- CATERPILLAR 3612LE
- CATERPILLAR 3612tE
- 454-bbl TANK BATlERY
- Date
- PROCESS FLOW DIAGRAM
- Designed By WY 610916
- LINDRITH COMPRESSOR STATION
- Drawn By WY 60916
- I Figure No
-
- Figure
-
- ENTERPRISE FIELD SERVICES LLC
- Checked By LDC 61016
- 3631170 -10708664
-
- 3631170 -10708664
- Approved By lOC 610116
-
- I Sheet of
-
- 1 1
- LINDRITH NEW MEXICO
-
- LINDRITH NEW MEXICO
- Table B-1 Project Emissions Summary (Criteria Pollutants) from Increased Condensate Throughput Lindrith Compressor Station Enterprise Field Services LLC
-
- ID
-
- ID
-
- ID
- EmlniON loune
- Deecrlpllon
- YOC
- HAh
- I Conctennt -jThroughput
-
- tPv
-
- tPv
- ~
- BbfV_r I
-
- TR
-
- Limits In Currnt Permit Number R6NM-03-R1
-
- TBATTERY
-
- TBATTERY
- Tanks
- Condensate Storage
- 3739
- 107
- 20000
-
- TLOAD
-
- TLOAD
- Truck Loading
- Truck Loading
- 223
- 007
- 20000
-
- MSS
-
- MSS
- MSS
- Maintenance Startup ShutdoMl
- 2500
- 064
- nla
-
- TR
-
- Total
- 6462
- 178
-
- Table
-
- TR
-
- Proposed Pennit Umlts
-
- TBATIERY
-
- TBATIERY
- Tanks Condensate Storage 10263
- 132
- 60000
-
- TLOAD MSS
-
- TLOAD MSS
- Truck Loading Truck Loading MSS Maintenance Startup Shutdown Tote -------shy-shy-498 2998 13759 -
- 014 059 205
- 60000 na
-
- Table B-2 Tank Emissions from Increased Condensate Throughput Lindrith Compressor Station Enterprise Field Services LLC
-