DIESEL PRODUCTION REFINERIES (PMR DPR) · PDF fileProxions Diesel Production Refineries...
Transcript of DIESEL PRODUCTION REFINERIES (PMR DPR) · PDF fileProxions Diesel Production Refineries...
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
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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.
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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
— 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.
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Manchester
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Trafford House
Chester Road, Manchester, UK
+44 (0) 161 8831706
London
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100 Brompton Road
Knightsbridge, London, UK
+44 (0) 20 339 785 07