proxion refineries
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CONDENSATE SPLITTERS (PMR-CS) PMR-CS-1 PMR-CS-5 PMR-CS-10 PMR-CS-20 PMR-CS-60 PMR-CS-120 PMR-CS-200 Design—Engineer—Install—Maintain
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CONDENSATE
SPLITTERS
Proxions Condensate Splitter (PMR-CS are com-
plete, modularized units ready for installation
and are designed to be fully erected and opera-
tional within 2-6 weeks from arrival at the pre-
pared project site. All equipment is fully warrant-
ed for 12 months and includes process guaran-
tee.
Our refineries work on a limited amount of
utilities and therefore or self sufficient depend-
ing on the crude type and product requirements.
Based on a typical 50° API) Condensate oil, the
PMR-CS will process the rated capacity and pro-
duce by volume approximately 50% Naphtha,
25% Distillate, and 25% Residuum.
Actual processing capacities, product percent-
ages and boiling points will vary depending on
the special characteristics of your crude. Upon
receipt of your crude composition.
Proxion Mini Refineries can also furnish any op-
tional equipment needed for further processing
of your product streams such as Distillate
Hydrotreaters, Catalytic Reformers, Vacuum
Units and Naphtha Stabilizers.
Products
____________________
NAPHTHA - Naphtha's boiling
end point is typically between
150°C (302°F) to 193°C (380°
F). This rough-cut hydrocarbon
will generally be blended back
with the residuum and re-
injected into the crude pipeline.
DIESEL (DISTILLATE) - This
product's typical boiling range
is from about 185°C
(365°F) to about 351°C (665°
F), and can be used as a heat-
ing oil and fuel. The unit will
produce arctic, winter and sum-
mer grades of diesel, depend-
ing upon the quality of the
crude.
RESIDUUM - The remaining
crude, which is heavier than
diesel, typically begins to
boil at about 287°C (550°F).
This product is generally blend-
ed back with the naphtha and
re-injected into the crude pipe-
line.
Capacities
____________________
Each PMR-CS is custom de-
signed to satisfy the client
unique requirement. Although
we do standardize our systems
so that addons can be imple-
mented quickly, safely and cost
effectively.
Most of our units can be
operated with a minimum turn-
down of 40% of maximum
throughput.
Standard Models :
— PMR-CS—1S
— 100 BPD
— PMR-CS—5S
— 500 BPD
— PMR-CS—10S
— 1000 BPD
— PMR-CS—20S
— 2000 BPD
— PMR-CS—60S
— 6000 BPD
— PMR-CS—120S
— 12,000 BPD
— PMR-CS—200S
— 20,000 BPD
Designation “C” after the model
number is for corrosive
environments.
Modular Construction
Complete with Modular Control Room and SCADA
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Standard Equipment
_________________________
Proxion Mini Refineries
provides completely
assembled process modules
containing all the necessary
equipment, piping, electrical
and instrumentation compo-
nents.
On-Module equipment in-
cludes:
— Heat Exchangers
— Furnace
— Pumps (100% Spared)
— Crude Tower
— Side Strippers (if
necessary)
— Air Coolers
— Accumulator Vessel
— Instrument Air
— Chemical Injection
— Product Sample Cooling
The Process Control System,
Safety Interlock System, and
Motor Control Center is prefab-
ricated and installed on module.
The unit can be controlled
locally and/or from a remote
control room.
Addons
____________________
— Desalter Modules
— Extra Draws offs
— Material upgrade for
corrosive crudes (C)
— API Pumps
— De-waxing units
— Gasoline Upgrading
— Desulpherization and
Merox units
STANDARD PMR-CS PROCESS FLOW
Process Description
__________________________________________________________________________
This PMR-CS is designed to separate the Condensate into several side cuts, an overhead
and bottom stream. The streams will be cut according to the boiling points pre-determined to
meet the product specifications and standard. The design of the process will be to operate at
a continuous state to the capacity outlined in the scope of supply for 330 days per year while
processing the condensate described in the assay provided. The plant will be modular and
skid mounted, incorporating the listed process equipment, piping, instrumentation and all
electrical junction boxes located at the skid edge. The PMR-CS does not use steam for strip-
ping, however steam stripping can be incorporated into the PMR-CS design as an add-on but
will be subject to design consideration and approval.
Condensate feedstock is delivered to the suction of the condensate charge pumps (by Buy-
er’s pipeline) from the outside battery limits, at the required minimum flow and suction
(NPSH) as required by the pumps. The condensate charge pumps, then delivers the conden-
sate to a pre-flash vessel where the light ends are flashed off and routed either to storage or
flare. The bottom liquid from the pre-flash vessel is delivered at the required pressure and
flow to the Atmospheric Distillation Column (ADU). The process in the column splits the con-
densate feed into the following products.
— Naphtha
— Kero/Jet Fuel
— Diesel
— Atmospheric Bottoms
The process is set up such that the side draw products will have a wide range of properties
(within limits) depending on the intended use. A side stream stripper might be envisaged for
the Naphtha, kerosene or diesel to remove the light ends from the products. The side stream
strippers will be envisaged based on specification and intended use.
Additional draw offs can be added if required.
DIESEL PRODUCTION REFINERIES (PMR-DPR) PMR-DPR-1 PMR-DPR-5 PMR-DPR-10 PMR-DPR-20 PMR-DPR-60 PMR-DPR-120 PMR-DPR-200 Design—Engineer—Install—Maintain
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DIESEL
PRODUCTION
REFINERIES
Proxions Diesel Production Refineries
(PMR-DPR) are complete, modularized units
ready for installation and are designed to be fully
erected and operational within 2-6 weeks from
arrival at the prepared project site. All equipment
is fully warranted for 12 months and includes
process guarantee.
Our refineries work on a limited amount of
utilities and therefore or self sufficient depend-
ing on the crude type and product requirements.
Based on a typical .865 gravity (32° API) crude
oil, the PMR-DPU will process the rated capacity
and produce by volume approximately 25%
Naphtha, 30% Distillate, and 45% Residuum.
Actual processing capacities, product percent-
ages and boiling points will vary depending on
the special characteristics of your crude. Upon
receipt of your crude composition.
Proxion Mini Refineries can also furnish any op-
tional equipment needed for further processing
of your product streams such as Distillate
Hydrotreaters, Catalytic Reformers, Vacuum
Units and Naphtha Stabilizers.
Products
____________________
NAPHTHA - Naphtha's boiling
end point is typically between
150°C (302°F) to 193°C (380°
F). This rough-cut hydrocarbon
will generally be blended back
with the residuum and re-
injected into the crude pipeline.
DIESEL (DISTILLATE) - This
product's typical boiling range
is from about 185°C
(365°F) to about 351°C (665°
F), and can be used as a heat-
ing oil and fuel. The unit will
produce arctic, winter and sum-
mer grades of diesel, depend-
ing upon the quality of the
crude.
RESIDUUM - The remaining
crude, which is heavier than
diesel, typically begins to
boil at about 287°C (550°F).
This product is generally blend-
ed back with the naphtha and
re-injected into the crude pipe-
line.
Proxion Mini Refineries can
also furnish any optional
equipment needed for further
processing of your product
streams such as Distillate
Hydrotreaters, Catalytic
Reformers, Vacuum Units and
Naphtha Stabilizers.
Capacities
____________________
Each PMR-DPR is custom
designed to satisfy the client
unique requirement. Although
we do standardize our systems
so that addons can be imple-
mented quickly, safely and cost
effectively.
Most of our units can be
operated with a minimum turn-
down of 40% of maximum
throughput.
Standard Models :
— PMR-DPR—1S
— 100 BPD
— PMR-DPR—5S
— 500 BPD
— PMR-DPR—10S
— 1000 BPD
— PMR-DPR—20S
— 2000 BPD
— PMR-DPR—60S
— 6000 BPD
— PMR-DPR—120S
— 12,000 BPD
— PMR-DPR—200S
— 20,000 BPD
Designation “C” after the model
number is for corrosive
environments.
3
www.proxionminirefineries.com
Standard Equipment
_________________________
Proxion Mini Refineries
provides completely
assembled process modules
containing all the necessary
equipment, piping, electrical
and instrumentation compo-
nents.
On-Module equipment in-
cludes:
— Heat Exchangers
— Furnace
— Pumps (100% Spared)
— Crude Tower
— Diesel Side Stripper (if
necessary)
— Air Coolers
— Accumulator Vessel
— Instrument Air
— Chemical Injection
— Product Sample Cooling
The Process Control System,
Safety Interlock System, and
Motor Control Center is prefab-
ricated and installed on module.
The unit can be controlled
locally and/or from a remote
control room.
Addons
____________________
— Desalter Modules
— Extra Draws offs
— Material upgrade for
corrosive crudes (C)
— API Pumps
— De-waxing units
— Desulpherization and
Merox units
STANDARD PMR-DPR PROCESS FLOW
Process Description
______________________________________________________________________
This PMR-DPR range is designed to separate the crude oil into several side cut,
bottoms and overhead streams by using atmospheric distillation process. The streams
will be cut according to the boiling points pre-determined to meet the product specifica-
tions and standards. The design of the process unit will be to operate at a continuous
state to the capacity outlined in the scope of supply for 330 days per year while pro-
cessing the crude oil described in the assay provided. The plant will be skid mounted
and modular designed including the listed process equipment, piping, instrumentation
and all electrical junction boxes located at skid edge. The PMR-DPR does not use
steam for stripping.
Crude oil feedstock is to be delivered to the suction of the crude charge pumps (by Buy-
er’s pipeline) from the outer battery limits, at the required minimum flow and suction
head (NPSH) as required by the pumps. The crude charge pumps, then deliver the
crude oil at required pressure and flow to crude distillation column. The process in the
column splits the crude feed into the following products.
— Naphtha
— Diesel
— Atmospheric Bottoms
The process is set up such that the side-draw diesel product can have a wide range of
properties (within limits) depending on the intended use. A side stream stripper column
is used to remove the light ends from the diesel product. The process is set up to blend
the kerosene with the diesel to maximise the diesel production.
Additional draw offs can be added if required.
HEAVY CRUDE PROCESSING REFINERIES (PMR-HCP) PMR-HCP-10 PMR-HCP-20 PMR-HCP-60 PMR-HCP-120 Design—Engineer—Install—Maintain
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HEAVY CRUDE
PROCESSING
REFINERIES
Proxions Heavy Crude Processing Refineries
(PMR-HV) are complete, modularized units ready
for installation and are designed to be fully
erected and operational within 4-8 weeks from
arrival at the prepared project site. All equipment
is fully warranted for 12 months and includes
process guarantee.
Based on a typical 20° API crude oil, the PMR-HC
will process the rated capacity and produce by
volume approximately 20% Naphtha, 25% Distil-
late, and 55% Residuum using Atmospheric dis-
tillation. The Naphtha and Diesel are then set to
storage while the Resid is further processed
using a Vacuum Distillation Unit (VDU).
Operating under Vaccuum allows for reduced
boiling points and further products can be yield-
ed. Standard products from the VDU are LVGO,
HVGO and VR.
Actual processing capacities, product percent-
ages and boiling points will vary depending on
the special characteristics of your crude. Upon
receipt of your crude composition.
Products
____________________
NAPHTHA
DIESEL (DISTILLATE)
LVGO
HVGO
VR
Proxion Mini Refineries can
also furnish any optional
equipment needed for further
processing of your product
streams such as Distillate
Hydrotreaters, Catalytic
Reformers, Vacuum Units and
Naphtha Stabilizers.
Capacities
____________________
Each PMR-HCP is custom
designed to satisfy the client
unique requirement. Although
we do standardize our systems
so that addons can be imple-
mented quickly, safely and cost
effectively.
Most of our units can be
operated with a minimum turn-
down of 40% of maximum
throughput.
Standard Models :
— PMR-HCP—10S
— 1000 BPD
— PMR-HCP—20S
— 2000 BPD
— PMR-HCP—60S
— 6000 BPD
— PMR-HCP—120S
— 12,000 BPD
Designation “C” after the model
number is for corrosive
environments.
Selected Case Study
____________________
Client
Phoenix International A/S
Client
Iraq
Work
FEED
Capacity
10,000 BPD
Crude — 17.8 API 4.59%
Sulphur
Modular Construction
Crude Distillation Unit (CDU)
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Standard Equipment
_________________________
Proxion Mini Refineries
provides completely
assembled process modules
containing all the necessary
equipment, piping, electrical
and instrumentation compo-
nents.
On-Module equipment in-
cludes:
— Heat Exchangers
— Furnace
— Pumps (100% Spared)
— Crude Tower
— Vacuum Distillation
Tower
— Stripper (if necessary
— Air Coolers
— Accumulator Vessel
— Instrument Air
— Chemical Injection
— Product Sample Cooling
The Process Control System,
Safety Interlock System, and
Motor Control Center is prefab-
ricated and installed on module.
The unit can be controlled
locally and/or from a remote
control room.
Addons
____________________
— Desalter Modules
— Extra Draws offs
— Material upgrade for
corrosive crudes (C)
— API Pumps
— De-waxing units
— Desulpherization and
Merox units
— Asphalt Blowers
STANDARD PMR- HCF PROCESS FLOW
Process Description
______________________________________________________________________
This PMR-HCP is designed to maximize the products slate from a heavy crude oil feed. The
PMR-HCP envisage the use of a crude distillation column and a vacuum distillation column to
separate the heavy crude into several side cuts, an overhead and bottom stream. The streams
from both the Crude Distillation Unit (CDU) and Vacuum Distillation Unit (VDU) will be cut
according to the boiling points pre-determined to meet the product specifications and standard.
The design of the process will be to operate at a continuous state to the capacity outlined in the
scope of supply for 330 days per year while processing the heavy crude oil described in the
assay provided. The plant will be modular and skid mounted, incorporating the listed process
equipment, piping, instrumentation and all electrical junction boxes located at the skid edge.
The PMR-HCP does not use steam for stripping, however steam stripping can be incorporated
into the PMR-HCP design as an add-on but will be subject to design consideration and approv-
al.
Heavy crude feedstock is delivered to the suction of the crude charge pumps (by Buyer’s pipe-
line) from the outside battery limits, at the required minimum flow and suction (NPSH) as re-
quired by the pumps. The crude oil charge pumps, then deliver the crude oil at required pres-
sure and flow to the CDU, where the process is split into an overhead, distillates side draws
and Atmospheric bottom. The Atmospheric bottom from crude distillation column is further
charged via an AR charge pump into the VDU at required pressure and flow, where the pro-
cess are further split into Light Vacuum Gasoil (LVGO), Heavy Vacuum Gasoil (HVGO) and
Vacuum Residue (VR).
The process in the PMR-HCP plant splits the crude feed into the following products.
— Naphtha
— Diesel
— LVGO
— HVGO
— VR
The process is set up such that the side draw products will have a wide range of properties
(within limits) depending on the intended use. Furthers side stream strippers maybe envisaged
for the CDU and VDU to remove the light ends from the products. The side stream strippers will
be envisaged based on specification and intended use.
Additional draw offs can be added if required.
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Manchester
__________________________
Trafford House
Chester Road, Manchester, UK
+44 (0) 161 8831706
London
__________________________
100 Brompton Road
Knightsbridge, London, UK
+44 (0) 20 339 785 07