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CORE TECHNOLOGY PLATFORM

Three Core Technologies Across Membrane Separation Engineering

Plum organizes PEK tubular membrane pretreatment, selective nanofiltration, and HRCC continuous concentration as independent or combinable technology modules around feed risks, target streams, and downstream interfaces, rather than as one fixed flowsheet that must always be reproduced in full.

Whether a project uses one, two, or all three technologies depends on feed composition, fouling and scaling risks, separation objectives, and final stream destinations.

Installed Plum industrial membrane system representing the core technology platform
From one membrane section to a combined routeInstalled systems, verifiable interfaces, and project-specific engineering boundaries

TECHNOLOGY PLATFORM MAP

Identify the engineering risk before deciding where a technology belongs

This map defines technology duties and interfaces. It does not mean every project requires every section, and industrial wastewater and production fluids do not share one parameter set.

  1. 01
    Water / process-fluid assessment

    Confirm source, variation, contaminants, target components, and downstream requirements.

  2. 02
    Front-end conditioning & solids separation

    Use reaction conditioning and PEK tubular membranes where required to establish a controlled feed boundary.

  3. 03
    Selective separation & purification

    Use membrane screening to define the two-stream relationship among targets, impurities, and the salt system.

  4. 04
    Continuous concentration where required

    Use HRCC to organize continuous RO concentration after pretreatment and feed-quality gates are satisfied.

  5. 05
    Downstream interfaces

    Reuse, resin, evaporation, crystallization, drying, or another project-defined final destination.

Combination principle:A technology enters the route only when it solves a defined project problem, not to complete a nominal full technology chain.

THREE ENGINEERING MODULES

Each technology controls a different engineering risk

Each technology states what it addresses, what it does not address, and which inputs it requires, keeping products, process solutions, and core technologies distinct.

01 PEK

PRETREATMENT & SOLID-LIQUID SEPARATION

PEK Tubular Membrane Pretreatment & Solid-Liquid Separation

Separate reaction solids, suspended matter, and compatible foulants under chemical-conditioning, high-solids, high-fouling, and demanding cleaning duties to establish a controlled feed for downstream membranes or resource recovery.

Primary duty
Solids separation for reaction solids, SS, colloids, oil, and highly fouling feeds
Does not replace
Dissolved-salt removal, complete organic treatment, or downstream refining
Required inputs
Contaminant form, conditioning, temperature, pH, cleaning, and downstream requirements

View PEK pretreatment technology

02 NF

SELECTIVE SEPARATION & FRACTIONATION

Selective Nanofiltration & Fractionation

Use size, charge, and feed-membrane interactions to establish project-specific passage, retention, and fractionation relationships in industrial wastewater salt systems and production-fluid target components.

Primary duty
Target-component fractionation, impurity control, salt separation, and purification interfaces
Cannot be assumed
Which side is the product, a fixed separation ratio, or salt quality
Required inputs
Complete composition, target stream, analytical method, material balance, and downstream operations

View selective nanofiltration technology

03 HRCC

CONTINUOUS RO CONCENTRATION

HRCC Continuous High-Concentration Reverse Osmosis

For suitably pretreated water and brine, organize continuous RO concentration through modular operation, online operating-state changes, and a complete water balance, then connect the section to reuse or a terminal process.

Primary duty
RO permeate recovery and concentrate minimization for compatible feed water
Does not replace
Front-end softening, organic control, evaporation and crystallization, or concentrate disposal
Required inputs
Scaling risk, organics, salt composition, operating pressure, and concentrate endpoint

View HRCC concentration technology

TWO APPLICATION PATHS

One technology platform, different duties in two business areas

Industrial wastewater starts from risk control and final destinations; process fluids start from target components, product quality, and downstream production operations.

INDUSTRIAL WASTEWATER

Industrial Wastewater Reuse, Minimization & ZLD

  1. Conditioning and PEK solids separation where required
  2. Selective NF routing according to the salt system
  3. HRCC concentration only after feed-quality gates are met
  4. Connect to reuse, evaporation and crystallization, or disposal

View industrial wastewater routes

PROCESS FLUID

Production-fluid clarification, fractionation & purification

  1. Define clarification or pretreatment around the target component
  2. Use selective NF to establish the two-stream relationship
  3. Use a project-specific concentration membrane section
  4. Connect to resin, chromatography, evaporation, or crystallization

View process-fluid routes

Process-fluid projects do not use HRCC by default, and industrial wastewater projects do not use the complete three-technology chain by default.

COMBINATION SCREENING

Five input groups determine how technologies are combined

Technology-route screening starts with project inputs and is narrowed through sample testing, continuous pilot validation, or relevant engineering evidence.

01

Feed & variation

Source, batch, flow, temperature, pH, viscosity, and operating cycle.

02

Fouling & scaling risks

Particles, oil, organics, hardness, silica, salt composition, and chemical effects.

03

Target streams

Components to retain, remove, pass, reject, or recover.

04

Downstream operations

NF, RO, resin, evaporation, crystallization, drying, or production reuse.

05

Final destinations

Product, reuse water, concentrate, by-product salt, sludge, or disposal interface.

Plum membrane sample-testing and pilot-validation platform
Validate technology combinations and engineering boundaries from sample screening through continuous pilot operation

VALIDATE BEFORE SCALE-UP

Technology combinations require evidence, not assembled universal parameters

When feeds are complex, target components are sensitive, or interfaces are uncertain, sample and pilot testing confirm membrane selection, stream identities, fouling and cleaning, water or material balances, and scale-up inputs.

  1. 01Data review
  2. 02Membrane & route screening
  3. 03Bench material balance
  4. 04Continuous pilot validation
  5. 05Scale-up design inputs

View sample-testing and pilot capabilities

CROSS-BUSINESS EVIDENCE

Cross-business records show how each technology enters an engineering route

Only confirmed capacities and technology sections are shown. Customer identity, performance, and new-project guarantees are not inferred here.

40 m³/h Coking wastewater with high silica and hardness

Reaction conditioning and PEK tubular membrane solids separation.

20 m³/h Lactic-acid NF purification

Selective NF fractionation and downstream refining interface.

52 m³/h Cooling-tower blowdown

PEK pretreatment and an HRCC RO section.

ENGINEERING FAQ

Core technology platform frequently asked questions

This overview screens technology duties and combinations. Parameters, equipment, and performance boundaries belong in the relevant detail page and project validation.

Submit a duty for technology-route screening

Must the three technologies be used together?

No. They may be used independently, in pairs, or as a complete chain where appropriate. Feed risks, separation objectives, downstream interfaces, and validation results determine the route.

Can PEK tubular membrane pretreatment remove dissolved salts directly?

No. It primarily separates reaction solids, suspended matter, and compatible foulants. Dissolved-salt control requires suitable NF, RO, or another process section.

Is selective NF permeate always the product stream?

Not necessarily. The target component may be in the permeate or retentate and must be confirmed through sample analysis, membrane screening, and a material balance.

Is HRCC suitable for every brine or production fluid?

No. HRCC requires suitable pretreatment, fouling and scaling control, membrane compatibility, and a defined concentrate endpoint. Suitability for a process fluid requires separate validation.

When are sample testing or pilot validation required?

Use sample testing and continuous pilot validation when component relationships, fouling and cleaning, selectivity, concentration boundaries, or scale-up remain uncertain.

Why does the overview omit universal performance parameters?

Operating windows and results depend strongly on the feed, pretreatment, and objective. Project records, test data, and new-project guarantees must remain separate and be confirmed in project documents.

ROUTE EVALUATION

Submit the duty to determine which technology belongs where

Provide feed analysis, treatment objectives, the current process, and final destinations for an initial review of technology duties and route combinations.