DRAWING NO:
PX-PID-001-REV A
| SCALE:
NTS
| DATE:
2025-08
TITLE:
PROCESS FLOW DIAGRAM / P&ID — 1 MGD MODULAR SYSTEM — ASPEN MODEL BASIS
CLASSIFICATION:
CONFIDENTIAL & PROPRIETARY
| PURIONEX WATER TREATMENT SYSTEMS
Legend
Process Line
Chemical/Dosing
Instrument Signal
Reject/Brine/Waste
Permeate/Product
Pump
Sensor/Transmitter
Control Valve
Control Bus
PRE-TREATMENT
CORE TREATMENT
POST-TREATMENT
CONTINGENCY / MODULAR ZONE
RAW WATER IN
S-01
P
P-101
STAGE 1
FT
FT-101
INFLUENT SCREENING
E-100 | 150–175 m³/hr
ASPEN: SPLIT [E-100]
T-101
SCREENINGS WASTE
S-02
STAGE 2
110VAC
IMT
INTELLIGENT MAGNETIC TREATMENT
E-200 | 2,000–8,000 Gauss
ASPEN: UDF [E-200]
S-03
pH
AT-101
STAGE 3
GAS SUPPLY
O₂ / O₃ / Air
C
K-301
DO
AT-301
NANO BUBBLERS
MICRO OXIDATION | <100nm
R-300 | 5–30 min contact
ASPEN: RCSTR/PFR [R-300]
S-04
P
P-301
STAGE 4
M-1
M-2
M-3
M-4
PT
PT-401
CIP/BW
T-401
UF CONCENTRATE
SUBMICRON FILTRATION
ULTRAFILTRATION | ≤ 0.1 µm | 4 Modules
MF-400 | TMP 0.5–4 bar | PVDF/PTFE
ASPEN: SEP/SPLIT [MF-400]
S-05
HP
P-501
STAGE 5
PV-501 (6 × 8"×40")
PV-502 (6 × 8"×40")
PV-503 (6 × 8"×40")
PT
PT-501
CT
CT-501
T-502
PERMEATE TANK
ERD
E-505
T-503
BRINE REJECT
REVERSE OSMOSIS
99.0–99.8% Salt Rejection | 75–85% Recovery
MEM-500 | 15–25 bar | BWRO TFC Polyamide
ASPEN: MEMBRANE [MEM-500]
S-06
STAGE 6
UV REACTOR
R-601
O₃ CONTACTOR
R-602
OZONE GENERATOR
K-601 | 0.5–5 kg/hr
UVI
AE-601
O₃ VENT
DESTRUCTOR
UV / OZONE (AOP)
ADVANCED OXIDATION | 4–6 log Reduction
R-600 | 40–400 mJ/cm² | 1–10 mg/L O₃
ASPEN: RCSTR/PFR [R-600]
S-07
pH
AT-601
CT
CT-601
STAGE 7
UPFLOW
CALCITE / COROSEX
D-701 | 50–100 mg/L Ca target
AT
AT-701
REMINERALIZER
POST-TREATMENT MINERAL RESTORATION
C-700 | CaCO₃/MgO | pH 7.0–8.5 | LSI 0 to +0.5
ASPEN: MIXER/RStoic [C-700]
S-PRODUCT
PRODUCT
WATER
T-800
50,000–100,000 gal
QT
QT-801
DISTRIBUTION
TO END USE
XV
XV-801
BYPASS / DCU DIVERT — ACTIVE ON: TDS >2500 ppm | pH EXCURSION | ORP SPIKE
STAGE 8
DCU — DYNAMIC CONTAINMENT UNIT
MODULAR | CUSTOM-ENGINEERED | DCU-800
SURGE
TANK
T-801
5,000–50,000 gal
VARIABLE RETENTION
EMRG
FILTER
F-810
GAC
C-820
IX-1
IX-2
ION EXCHANGE
pH NEUT
TANK
T-840
ACID
BASE
T-851
T-852
MOBILE DOSING
pH
ORP
TDS
AT-800 ARRAY
ASPEN: RCSTR / Flash2 / RStoic / UDF (ASPEN Dynamics) [DCU-800]
RETURN
TO PROCESS
AI / PLC / SCADA CONTROL LAYER
FlowSignal™ AI | ASPEN Plus Digital Twin | 4–20mA / HART / Modbus / Profibus | PLC-001 (Rockwell / Siemens S7)
ASPEN MODEL BLOCK SUMMARY —— PROPERTY METHOD: ELECNRTL (Electrolyte NRTL) —— ENERGY: AEA
E-100 Influent Screening SPLIT
E-200 IMT Custom UDF
R-300 Nano Bubblers RCSTR / PFR
MF-400 Submicron Filtration SEP / SPLIT
MEM-500 Reverse Osmosis MEMBRANE block
R-600 UV / Ozone AOP RCSTR / PFR
C-700 Remineralizer MIXER / RStoic
DCU-800 Dynamic Containment Flash2 / UDF (Dyn.)
Design: 1 MGD | 150–175 m³/hr | 80/20 Modular
RO Feed: SDI <3 | Turbidity <0.1 NTU
RO Peerm: TDS 10–50 mg/L | pH 5.5–7.0
Product: TDS 50–200 mg/L | pH 7.0–8.5 | LSI 0–+0.5
Brine Rej: TDS 3,000–20,000 mg/L | ERD energy recovery
Screenings: Solids to waste | LCA carbon tracked
DCU Bypass: Activated on threshold exceedance — returns to process
Energy: 0.05–4 kWh/m³ stage-dependent | ERD + VFDs
ASPEN Plus: Steady-state process model + sensitivity
ASPEN Dynamics: DCU surge | transient states | control
AEA: Capital + operating cost optimization
Digital Twin: FlowSignal AI synced to ASPEN in real-time
Prop. Method: ELECNRTL | electrolyte + membrane systems
LCA: Embedded carbon accounting in all streams
Reg. Baseline: EPA / WHO / NSF-61 cross-validated
Next Steps: Pilot critical components | N+1 redundancy
S-01 Raw Water In 500–5,000 mg/L TDS
S-02 Post-Screen Coarse solids removed
S-03 Post-IMT Scale precursors altered
S-04 Nano-Oxidized Fe/Mn oxidized, DO elevated
S-05 UF Permeate (RO-ready) SDI<3 | <0.1 NTU
S-06 RO Permeate TDS 10–50 mg/L
S-07 AOP-Treated 4–6 log pathogen reduction
S-PR Product Water Potable quality distributed