Frac Vap Water Treatment Unit Gas Frac Condenser Unit

Potable water is produced

through Flash Evaporation & Condensation

following recovery of solids as retail chemical products

and return of crude oil to the client.

Recovery

of C2, C3, C4

& C5 as pure liquid

fuels (NGLs) and LMG (C1) from Shale Gas

Frac Vap, ßio-ßol & Gas Frac Technologies

TRANSFORMATIVE

TECHNOLOGIES FOR

THE FRACKING

INDUSTRY

WORLDWIDE

Western Frac Vap Corporation Frac Vap, ßio-ßol & Gas Frac Technologies

Timeline of Inventions & Achievements Frac Vap, Gas Frac & ßio-ßol

2011

2012

2013

2015

2016

2014

THERMO WRAP, patented by Garry Bush for

energy conservation in residential air-conditioning

GAS RECOVERY SYSTEM, novel cryogenic LPG system designed by

Garry Bush and patented by his client, was commissioned in 2012

without incident or delay and has been fully operational ever since.

FRAC VAP designed and patented by Garry Bush for

treatment of Flow Back from Hydraulic Fracking

GAS FRAC designed and patented by Garry Bush for separation

and recovery of NGLs present in Shale Gas (ethane, propane,

butane & pentane).

ISLAM MAGDY SAYED, mechanical engineer

(Multi-Stage Flash Desalination) was introduced to

Garry Bush through O&G establishment in Alberta.

ßIO-ßOL (Serena Domvile) is incorporated into both Frac Vap and

Gas Frac to reduce costs & greatly broaden commercial benefits.

COMMERCCIAL LAUNCH (JULY 2016)

3 Founding Principles

■ Control Volume = Containerized Units

■ Refrigeration Technology = Energy Conservation

■ Latent Heat Management

■ Rigorous Environmental Management

Frac Vap and Gas Frac (including ßio-ßol) use “Control

Volumes” or Containerized Units to capture sensible heat as

latent heat, significantly lowering make-up (sensible) energy

requirements

relative to

competing

technologies. Incoming sensible heat is

circulated in refrigerant-containing solutions in

both cases. Water towers control the phase

transitions of water in the Frac Vap and gas

transitions in the Gas Frac case. ßio-ßol,

similarly, uses “containerized” bio-filtration

media to control the metabolism of

immobilized microbes responsible for the

fixation of CO2 and removal of organic and inorganic “nutrients” from gas and water

streams.

Sensible

heat

introduced

with Shale

Water and

Shale Gas

is stored in

circulating

solution

and

released as

available

energy for

respective

processes.

Fra

ckin

g R

eagen

ts

&

Internal Power

Generation

Frac Vap, ßio-ßol & Gas Frac Transformative Technologies for O&G Industry

Two technologies can be operated in unison as depicted simplistically above,

with methane vapour used to fuel the GENSET for the two units.

Frac Vap Gas Frac

Shale Gas

Shale Liquid

CO2e Credits

Bio-Fuel

GENSET

Crude Oil

Drilling Reagents

Potable Water

Liquid Methane Gas (LMG)

Liquid Ethane

Liquid Pentane

Liquid Propane

Liquid Butane

CO2 & H2 Gas

H2O &

Solids

LMG5 & LMG10

Gas Frac & ßio-ßol PSA & NGL and LMG Condenser

Frac Vap & ßio-ßol

5 Frac Vap/ßio-ßol & Gas Frac Processes, Products & Performance FRAC VAP

ICON Process

Product Method of Recovery

Process

Efficiency Destination

Crude Oil

Principles of mass flow dynamics

followed by carbon adsorption w/o

need for solvent extraction

Over 90% Return to Client

Potable Water

Removal of TSS & TDS using

centrifugation, flocculation and

macro/micro- and bio-filtration;

Flash Evaporation & Condensation

of H2O Potable Water

Over 90% Recovery

(TDS = 0)

Reuse in Hydraulic

Fracking and/or Sale

as Drinking, Irrigation

or Industrial Water

Reagent-Grade

Drilling Reagents

Combining. Drying and mechanical

sieving of TSS & TDS

> 90% recovery;

>99.9% purity

Commercial-Grade

Products for Sales or

Reuse in Hydraulic

Fracking

GAS FRAC

ICON Products Method of Recovery Process

Efficiency Destination

Liquid Ethane

Propane, Butane &

Pentane

Cooling of Heat Exchangers =

Dew Points of Gases

Over 90% recover;

over 99% purity of

separated liquid gases

Commercial NGL

Sales

Liquid Methane

Gas (LMG)

Separatioon of methane vapour

from ethane, propane, butane and

pentane using molecular sieving

prior to dew point condensation

Over 99% recovery

LMG (pure methane

gas) and LMG5 and

LMG10 (5 and 10%

ethane addition)

Carbon Credits

GWP = 25

(GWP of

CO2 = 1)

ßio-ßol Technologies

Over 90% fixation of

CO2 from power

generator and shale

gas

CO2e Credits for

Removing CO2 and

CH4 from Tail Gas

through bio-filtration

Burning of CH4: CH4 + 2O2 CO2 + 2H2O + energy

GWP: Global Warming Potential

Frac Vap Unit Recovering Liquid Phase as Potable Water, Crude Oil and Solids

(TSS & TDS) as Commercial Products for Sale or Internal Use

FLOW

BACK Cyclones & Centrifuges

Oil Extraction TSS Removal

“Warm”

Flocculation

Macro & Micro-

Filtration

Bio-

Filtration

Ion-

Exchange

Pall

Filters

Flash

Evaporation

“Flash”

Condensation

Potable

Water

Dryer for

Solids

Mechanical

Sieving

Calcium &

Sodium Salts

Potassium

Salts

Nitrogen, Phosphorus

Oxides & Salts

Friction Reducers

and Polymers

Crude Oil

Carbon

Credits

Bio-Fuel

H2S

Removal

Solvent extraction &

charcoal filtration

7 Gas Frac Unit Recovering Shale Gas Vapours as NGLs

& Liquid Methane Gas (LMG) plus CO2e Credits

A - Pressure Swing Adsorption Unit

Fixed as Biomass & CO2e Credits

COALESCER #5

Liq

uid

Gas

Sal

es

Dump Tank #1

Liquid Pentane

Pal

l Filt

er

Ho

ldin

g T

anks

Dump Tank #2

Liquid Propane

Dump Tank #3

Liquid Butane

Dump Tank #5

Liquid Ethane

COALESCER #2

Ext

ract

ion

of

Bio

-Fu

el SHALE GAS

Hydraulic Fracking and O&G well development

C3H8 C4H10 C5H12 H2O Solids C2H6

COALESCER #1

Heat Exchanger #5

1

2

3

WATER TOWER(S)

N2 CO2 H2 CH4

Heat Exchanger #2

Heat Exchanger #1

Dump Tank #4

Liquid Methane

Heat Exchanger #4

Heat Exchanger #3

COALESCER #3

COALESCER #4

B – Dew Point Condensation of Separated Vapors

Separated Gas Vapors

Pre-Filter Removed

removed

4

5