Safe Tank Truck Loading Alternatives€¦ ·  · 2017-11-08Safe Tank Truck Loading Alternatives ....

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Transcript of Safe Tank Truck Loading Alternatives€¦ ·  · 2017-11-08Safe Tank Truck Loading Alternatives ....

Page 1: Safe Tank Truck Loading Alternatives€¦ ·  · 2017-11-08Safe Tank Truck Loading Alternatives . Why are we here today ... Can be combined with a scavenger system to reduce H2S
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Safe Tank Truck Loading Alternatives

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Why are we here today

Oxygen and VOC problems encountered in

today’s truck loading environment

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Loading Options

• Free venting and purging

• Vapor balancing

• Vapor burning (combustion)

• Vapor recovery

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Free venting and purging

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Typically a facility's air permit is

limited to 50 tons or less of VOCs

annually.

The issue: Loading one 200 barrel

truck per day and venting the gases

into the atmosphere consumes 14.8

tons of the 50 ton annual limit or

30%.

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The issue: Heath and Safety in the

loading rack area becomes apparent

in terms of vapor clouds that are

explosive and contain carcinogens.

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Vapor Balancing

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Facilities are typically limited to 10

ppm per ft3 of O2 in the natural gas

sales pipe line.

The issue: Vapor balancing a 200

barrel load to a storage tank (to

reduce emissions) will on average

inject 16 ft3/min of a 124,000 ppm

O2/hour.

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Vapor burning (combustion)

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Page 18: Safe Tank Truck Loading Alternatives€¦ ·  · 2017-11-08Safe Tank Truck Loading Alternatives . Why are we here today ... Can be combined with a scavenger system to reduce H2S
Page 19: Safe Tank Truck Loading Alternatives€¦ ·  · 2017-11-08Safe Tank Truck Loading Alternatives . Why are we here today ... Can be combined with a scavenger system to reduce H2S
Page 20: Safe Tank Truck Loading Alternatives€¦ ·  · 2017-11-08Safe Tank Truck Loading Alternatives . Why are we here today ... Can be combined with a scavenger system to reduce H2S
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Facilities are stressed to add

combustion products to a

production facility

The issue: Re-permitting, finding

available safe real-estate, lost

revenue, and public perception.

.

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Vapor recovery

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Note higher removal efficiencies can be achieved if requested.

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Recovery Calculation 14 gal per

200 barrel truck load

0.00

10.00

20.00

30.00

40.00

50.00

60.00

Va

po

r C

on

ce

ntr

ati

on

Recovery rate per 1000 gal loaded

Recovery Rate per 1000 gallons loaded

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A carbon based Vapor recovery unit

eliminates re-permitting, HSE and oxygen

shut in issues while providing an

attractive ROI.

The issue: The initial CAPEX is large

when compared to flaring alternatives.

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Advantages

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Oxid

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/ T

ruck

Lo

ad

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N

atu

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ncl

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N

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n/C

O2

Pu

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Air

Defe

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(Carb

on

Bed

Vap

or

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cov

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)

Familiar technology X X X

Minimal foundation requirements X

Low installation cost X X

Low CAPEX X X

Fully automated X X X X X

Minimal maintenance X X X

Removes odor X X X X

Can be combined with a scavenger system to reduce H2S X X X X

Low Noise X X X X

No Visible Flame X X X X

Minimal HAP release X X

+99% DRE X NA NA

No assist or purge gas required X X

Flameless operation X X

Recovers product X

Easily scalable/ modular design X

Can be installed in a Class 1 Div 2 area(panel unclassified and remote mounted)

X

No production of NOX CO or CO2 X X

Can meet +99% VOC reduction to meet EPA Control device not affecting permit

X

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Disadvantages

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En

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Fla

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Oxid

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ruck

Lo

ad

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Natu

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Nit

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/CO

2 P

urg

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A

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(Carb

on

Bed

Vap

or

Reco

very

)

Possible smoke X X X

Noise X

Visible flame/ Negative public perception X

Requires Nitrogen or Natural Gas purge prior to start up during

operation and shut down X X

98% DRE X X

Potential for flashback explosions X X

Location on site requires safe area X X X

Affects air permitting X X X

Emits CO NOX CO2 X X X

Lost revenue by burning product X X X

Requires significant fuel gas/ High operating cost X X

Higher maintenance X

Larger footprint X

Initial CAPEX X X X

Heat trace required for vacuum pump to storage tank

X

Noted as not desired at Midstream sales point X

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Initial cost Power usage Pilot gas usage Assist gas usage liquid recovered product Operational costs per yr

Elevated Flare operating 24 hrs per day $ 36,000.00 12 KW 1440 SCF 9216 SCF N/A $ (11,669.00) .

Enclosed Flare operating 12 hrs per day $ 32,000.00 12 KW 720 SCF 7400 SCF N/A $ (8,891.00)

Enclosed Combustor operating 12 hrs per day $ 125,000.00 60 KW 720 SCF 30000 SCF N/A $ (35,390.00)

Carbon Vapor recovery operating 24 hrs per day $ 215,000.00 192 KW N/A N/A 168 gal $ 89,294.00

Assumptions

1. Loading twelve 200 barrel trucks in a 24 hour period (truck load time 1 hr.)

2. Natural gas costs at $3 per 1000 ft3

3. Power costs at 8 cents per KW hour

4. Crude costs at $65/barrel

`

Typical capital and operations costs

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