the esmil approach

Esmil Presentation At
PRODUCED WATER WORKSHOP
ABERDEEN
Esmil Process Systems Ltd
DEV CHABBA
JUNE 8 - 2016
Esmil Process Systems Capability Statement
INTRODUCTION
• Esmil Process Systems Ltd
• Membrane Concept, different types of
Membranes
• Pilot Plant Approach
• Ultra High Pressure RO for secondary
enhanced recovery
• Discussion
Esmil Process Systems Capability Statement
COMPANY HISTORY
• Formed in 1978
• Awarded Queens Award for the Environment
Achievement in 1999 for the “Zero Discharge Process”
• DTI best supplier award in 2000
• 2012 Esmil supply specialist plant to Halliburton in PNG
• 2012 Esmil awarded large project for BTEX and
Hydrocarbon removal from effluent stream
• 2013 Waste water treatment and recovery plant in Russia
• 2015 Esmil complete largest project so far at over £5.0
million for Shell E&P at Corrib.
Esmil Process Systems Capability Statement
EXTENSIVE MEMBRANE
EXPERIENCE
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ULTRAFILTRATION
NANOFILTRATION
REVERSE OSMOSIS
VSEP (Vibratory Shear Enhanced Process)
CERAMIC MEMBRANES
Esmil Process Systems Capability Statement
WASTE WATER TREATMENT
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Industrial Effluent treatment
Oily Waste Water treatment
Produced Water Treatment
Gas Condensate Treatment
Refinery Waste Water Treatment
Esmil Process Systems Capability Statement
PROCESS CAPABILITY
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MEMBRANE SPECIALISTS, UF/NF/RO
VSEP (Vibratory Shear Enhanced Process)
Detailed Process Design
Detailed Engineering Design and Specification
Equipment Procurement Supply and Installation
Commissioning and Operation
Esmil Process Systems Capability Statement
Membranes Simplified
Esmil Process Systems Capability Statement
Esmil Process Systems Capability Statement
THE ESMIL APPROACH
• The Laboratory Scale Test Evaluation
• The Pilot Plant Site Trials for New
Applications
• The Design Team and Engineering Team
• The Project Team
• The Installation and Commissioning Team
Esmil Process Systems Capability Statement
Spiral and VSEP Pilot Plants
Esmil Process Systems Capability Statement
Esmil Process Systems Capability Statement
Esmil Process Systems Capability Statement
Esmil Process Systems Capability Statement
Parameter
Design
Design
Design
Composition Composition Composition
PW-A
PW-B
PW-C
Treated
Water
EQS
Sodium (mg/l)
23050
28174
8
Potassium (mg/l)
3106
1376
0.1
Calcium (mg/l)
2050
2410
98
Magnesium (mg/l)
737
272
1
Barium (mg/l)
0.4
3.25
1
0.5
Dissolved Iron (mg/l)
185
38.25
-
1
Chloride (mg/l)
41200
49365
100
Sulphate (mg/l)
4093
85.5
6
Bicarbonate (mg/l)
195
1.25
0
4
8.1
0.43
2
Aluminium (mg/l)
1.3
0.18
0.1
0.2
Silicon (mg/l)
4.6
2.8
0.1
1
0.8
0.4
2.3
7
0
Boron (mg/l)
Phosphorus (mg/l)
Lithium (mg/l)
Parameter
Design
Design
Design
Composition Composition Composition
PW-A
PW-B
PW-C
Treated
Water
EQS
Chromium (mg/l)
0.5
1.24
0
0.1
Manganese (mg/l)
3.1
5.13
2.54
0.3
Nickel (mg/l)
15.7
0.19
0.1
Copper (mg/l)
0.44
0.43
0.05
Zinc (mg/l)
25
16.4
Arsenic (mg/l)
0.5
0.003
0.05
Selenium (mg/l)
0.1
0.001
0.02
Silver (mg/l)
0.1
0.0013
0.01
Cadmium (mg/l)
0.05
0.013
0.005
Mercury (mg/l)
1
0.00004
0.0001
0.5
1.51
0.005
0.03
0.01
Lead (mg/l)
Tin (mg/l)
Oil, Fat & Grease
(mg/l)
15
15
3.83
15
0.1
0.3
Parameter
Design
Composition
PW-A
Design
Composition
PW-B
Phenol (mg/l)
10
0.00025
Ammonia (mg/l)
5
0.3
BTEX (mg/l)
25
0.01
PAH (mg/l)
1
0.0008
Methanol (mg/l)
150
150
150
TOC (mg/l)
200
200
200
COD (mg/l)
500
500
Suspended Solids (mg/l)
320
320
320
Visually
Neutral
4.8 to 7.4
4.56
4.56
6 to 9
TDS (mg/l)
76000
81900
250
SG
1.053
1.053
1.0001
pH
*
TOC includes methanol
Design
Composition
PW-C
Treated
Water
EQS
0.0005
0.0002
150*
400
AS BUILT PLANT PHOTOS
Esmil Process Systems Capability Statement
Corrib Project Over view
Esmil Process Systems Capability Statement
Membrane Skid for
Corrib Project
Esmil Process Systems Capability Statement
Corrib Project As Built
Esmil Process Systems Capability Statement
ULTRA HIGH PRESSURE RO
• Dow Water and Process Launched and
Successfully Tested UHP RO Membrane in
2015.
• Esmil and Dow Working on Concept to
Reduce the Concentrate Volumes of Existing
RO Systems to Enable Higher Recovery
Optimisation.
Esmil Process Systems Capability Statement
Example: 60 m3/h
UHPRO Plant
Stage 1
BWRO
60m3/h
30 bar
TDS: 1.3%
Stage 2
SWRO
Stage 3
UHPRO
Permeate
39 + 8 + 5 m3/h
65% recovery
40% recovery
21 m3/h
75 bar
TDS: 3.6%
Break
tank
1 vessel in the scheme stands for, 6 elements each
12.5 m3/h
120bar
TDS 6%
18 elements
@ 13 L/m2/h
36+24 elements
@ 18.6 L/m2/h
40% recovery
24 elements
@ 8 L/m2/h
Break
tank
Concentrate/Brine
7.5 m3/h
Final TDS: 10%
(To thermal
treatment)
ANY QUESTIONS
?
Esmil Process Systems Capability Statement