Skip to content

Application

Zero liquid discharge without an evaporator on the whole flow

A membrane route to ZLD compliance that carries the stream to crystallization-ready concentration, so the thermal stage is sized only for what is left.

Rows of reverse-osmosis pressure vessels in a bright treatment hall
Lower energy and capital than thermal
60–75%
Overall water recovery
99%+
Smaller footprint
70%
Concentration before crystallization
280g/L

Why ZLD projects stall

The two established routes each fail a different way. The stream between their limits is a concentration duty, not an evaporation duty.

Concentration ceiling
Conventional RO
≈90,000 mg/L
Thermal alone
No technical limit
The membrane train
280,000 mg/L
Specific energy
Conventional RO
2.7–4 kWh/m³
Thermal alone
25–60 kWh/m³
The membrane train
≤12 kWh/m³
Thermal duty
Conventional RO
Still required on the whole flow
Thermal alone
The entire stream is boiled
The membrane train
The residue only
The outcome
Conventional RO
Cannot reach ZLD
Thermal alone
Economically prohibitive
The membrane train
Compliance within the plant's economics
Routes to zero liquid discharge compared
Conventional ROThermal aloneThe membrane train
Concentration ceiling≈90,000 mg/LNo technical limit280,000 mg/L
Specific energy2.7–4 kWh/m³25–60 kWh/m³≤12 kWh/m³
Thermal dutyStill required on the whole flowThe entire stream is boiledThe residue only
The outcomeCannot reach ZLDEconomically prohibitiveCompliance within the plant's economics

Where the mandates bind

Water-stressed regions in the Middle East are tightening discharge limits without a single federal date; US state-level requirements are expanding alongside the federal rule.

China2019Coal power, chemicals, textiles, manufacturing
India2022Textile, chemical, and thermal power plants
European Union2023–2025Industrial Emissions Directive, major industrial sectors
United States2029EPA flue-gas desulfurization compliance for coal power
202020252030today

ZLD rules in force from

Zero liquid discharge mandates by jurisdiction
JurisdictionBinding fromCovers
China2019Coal power, chemicals, textiles, manufacturing
India2022Textile, chemical, and thermal power plants
European Union2023–2025Industrial Emissions Directive, major industrial sectors
United States2029 (emerging)EPA flue-gas desulfurization compliance for coal power

The range that has always required an evaporator

Conventional RO stops at about 90,000 mg/L. A crystallizer wants a feed several times more concentrated than that.

Conventional RO2.7–4 kWh/m³
MemBrine Concentrator™5–12 kWh/m³
Evaporation and crystallization25–60 kWh/m³
0100k200k300k

mg/L TDS

  • 35,000 mg/LSeawater
  • 90,000 mg/LConventional RO limit
  • 280,000 mg/LMemBrine Concentrator™ ceiling
Operating ranges by lane (mg/L TDS)
LaneRangeFrom (mg/L TDS)To (mg/L TDS)Note
MembraneConventional RO090,0002.7–4 kWh/m³
MembraneMemBrine Concentrator™90,000280,0005–12 kWh/m³
ThermalEvaporation and crystallization90,000300,00025–60 kWh/m³

The membrane ZLD train

Three membrane stages carry the stream to crystallization-ready concentration, so the thermal unit at the end is sized only for what is left. The bulk of the water leaves at the front, at the cheapest point on the curve; the last water is the expensive water.

The generic train; each project's design basis sets the actual streams. The same drawing with the measured King Salman Park numbers is on the case study.

Osmosys membrane scope1234Difficult feedPretreated per chemistrySEBRO™Semi-batch RO→ 25,000 mg/LSAMRO™Salinity-adaptive→ 90,000 mg/LMBC™Brine concentrator→ 280,000 mg/LCrystallizationSized for the residueRecovered water99%+ of feed5Minimal solidsThe residue only6
  1. 01Feeddifficult industrial water; pretreatment set by the chemistry
  2. 02SEBRO™ concentrate25,000 mg/L
  3. 03SAMRO™ concentrate90,000 mg/L
  4. 04MBC™ concentrate280,000 mg/L · 5–12 kWh/m³
  5. 05Recovered water99%+ of the feed, across the train
  6. 06Solidscrystallizer sized for the residue only
Process flow diagram with stream table
StreamNameDetail
1Feeddifficult industrial water; pretreatment set by the chemistry
2SEBRO™ concentrate25,000 mg/L
3SAMRO™ concentrate90,000 mg/L
4MBC™ concentrate280,000 mg/L · 5–12 kWh/m³
5Recovered water99%+ of the feed, across the train
6Solidscrystallizer sized for the residue only
A thermal evaporator and crystallizer plant - the equipment the membrane train sizes for the residue only

When the permit still allows some discharge

Recovery in the mid-nineties, with a much smaller thermal stage at the end of the train.

Minimal liquid discharge is the honest answer where a permit allows some discharge and full crystallization cannot yet be justified. The same train delivers it, with the last stage left out and added later.

A first read on your stream

Send the flow, the chemistry, and the target. A process engineer replies with a first read on recovery, energy, and the train worth piloting.