HEDROTEC Technology Platform

A technology platform for modular water reuse.

Proven components. Proprietary integration.

HEDROTEC combines process engineering, biological treatment integration, membrane integration, proprietary reactor architecture and digital operations into modular systems for water recovery and reuse.

The platform is designed around site-specific water conditions, practical deployment and a pathway from engineering to repeatable products.

Patent-Pending Vertical Reactor Architecture German patent application DE 10 2026 001 174.4 filed — examination pending.
Platform layers

Six technology layers. One integrated platform.

  • 01 — Process EngineeringFeed characterization, conditioning strategy and process selection based on actual water conditions.
  • 02 — Biological Treatment IntegrationCompact biological treatment integrated as an application-specific process layer for organic-load reduction, where required.
  • 03 — Membrane IntegrationSupplier-neutral membrane selection and integration as a separation component within the overall treatment architecture.
  • 04 — Hydrostatic Filtration ConceptsHydraulic head can be used as a design lever to reduce pumping demand in suitable project configurations.
  • 05 — Vertical Reactor Architecture — Patent PendingA compact proprietary reactor architecture developed for integrated treatment functions and modular deployment.
  • 06 — Digital & AI OperationsA monitoring and decision-support layer connecting process instrumentation to predictive operation and operating guidance.

These technology layers represent HEDROTEC’s engineering capabilities and are combined according to each application. They do not represent a fixed treatment sequence.

HEDROTEC platform architecture, six conceptual layers Six engineering layers of the HEDROTEC technology platform: process engineering, biological treatment integration, membrane integration, hydrostatic filtration concepts, vertical reactor architecture, and digital operations. The arrangement is conceptual and does not represent process sequence or reactor configuration. 01 — PROCESS ENGINEERING Water characterization & process design 02 — BIOLOGICAL TREATMENT Application-specific, where required 03 — MEMBRANE INTEGRATION Supplier-neutral separation integration 04 — HYDROSTATIC FILTRATION Hydraulic-head design concept 05 — VERTICAL REACTOR Patent-pending architecture 06 — DIGITAL & AI OPERATIONS Observation, prediction & decision support

Conceptual technology layers — not a process sequence or reactor configuration.


Pillar 02 · in depth

Biological treatment integration.

Biological treatment is integrated where the wastewater matrix and reuse objective require biological conversion. HEDROTEC defines the biological process around organic loading, biomass retention, oxygen demand, hydraulic conditions and the requirements of downstream treatment.

Biomass retention

Attached-growth concepts can support stable retention of active biomass within compact treatment volumes.

Load adaptation

Biological design responds to organic load, hydraulic variation and the characteristics of the actual wastewater matrix.

Aeration & oxygen transfer

Aeration strategy is evaluated against oxygen demand and process conditions — reduced specific aeration demand is a design objective, not a guaranteed outcome.

Modular integration

Biological treatment is integrated with upstream and downstream process functions, not engineered as an isolated unit operation.

Overhead view of an industrial biological wastewater treatment and aeration basin

Representative biological-treatment and aeration context — final process configuration is application-specific.


Pillar 03 · in depth

Membrane integration.

Membranes are integrated as one separation component within the overall treatment architecture. Selection and operating strategy are defined by water quality, treatment objectives and project conditions.

Ceramic membrane filtration, cross-section Feed water flows toward a submerged ceramic plate. Suction draws clean permeate through 0.10 micron pores into an internal channel and out as recovered water, while rejected solids are periodically purged as concentrate. FEED WATER CERAMIC MF · ~0.1 µm REFERENCE PORE SCALE PURGE — CONCENTRATE CONTROLLED SUCTION ≈ −0.2 bar target PERMEATE OUT

Outside-in suction filtration through a submerged flat-sheet ceramic plate


Surface characterization

Membrane surface characterization by AFM.

Atomic force microscopy (AFM) reveals membrane surface topography and relative roughness at the micro- and nanoscale. The resulting surface maps support comparative assessment of material characteristics relevant to membrane selection, integration and application-specific cleaning strategy.

  • Surface topography— maps local height variation across the membrane surface
  • Roughness comparison— enables relative comparison of surface texture characteristics
  • Engineering use— supports material screening and application-specific membrane evaluation

Representative AFM-based surface characterization images used for comparative material understanding and engineering evaluation.

Reference configuration

Project-specific membrane configuration.

ParameterValue
Membrane technologyCeramic flat-sheet MF, where selected
Installation conceptSubmerged configuration
Membrane areaSized per application
Operating conditionsDefined by feed water and treatment objective
Cleaning strategyFeed- and fouling-specific

Final membrane technology, configuration and supplier are selected for each project. HEDROTEC engineers the surrounding process architecture, hydraulics, controls and operating strategy.

Membrane operations

Operating strategy adapted to the application.

Filtration

Permeate withdrawal is controlled according to feed conditions and the selected membrane configuration.

Air scour

Used where required to support surface control and stable membrane operation.

Backwash

Applied according to hydraulic performance and fouling behavior.

CIP

Cleaning chemistry and frequency are defined by the dominant fouling or scaling mechanism.

Membrane sourcing

Specialist membranes. Integrated by HEDROTEC.

HEDROTEC does not manufacture membrane material. Where membrane filtration is selected, specialist membrane technology is chosen according to the application and integrated into the complete treatment system.

Our engineering scope focuses on the surrounding process architecture — pretreatment, hydraulics, controls, solids management and operating strategy — to ensure the selected membrane technology works reliably within the overall system.

  • Supplier selection— project-specific, based on application requirements
Membrane technology
Selected per project
Specialist membrane supplier chosen according to application and integration requirements

Pillar 04 · in depth

Hydrostatic filtration concepts.

Where site elevation and tank layout allow it, available hydraulic head may support permeate withdrawal and reduce the required active suction — a design lever evaluated per site, not a universal substitute for pumped filtration.

This is a general filtration and system-design concept evaluated across HEDROTEC platforms — not a disclosure of the patent-pending Vertical Reactor's internal construction.

Hydrostatic head concept, schematic A feed source held at elevation creates an available hydraulic head, marked as delta h, above a lower membrane process point. That head may support permeate withdrawal and reduce — not eliminate — the active suction required, shown as a smaller supplemental suction component downstream. FEED SOURCE Elevated vs. process point Δh AVAILABLE HEAD PROCESS / MEMBRANE POINT Lower elevation PERMEATE, HEAD-ASSISTED SUPPLEMENTAL ACTIVE SUCTION HYDROSTATIC FILTRATION CONCEPT — SCHEMATIC, NOT TO SCALE

Available hydraulic head may support permeate withdrawal and reduce required active suction where technically feasible — not a zero-energy or universally gravity-only filtration claim.


Pillar 05 · in depth — Patent Pending

Vertical reactor architecture.

Treatment functions — including biological treatment where required by the application — can be integrated within a vertically organized reactor architecture to reduce footprint and support modular deployment. The proprietary internal configuration is the subject of German patent application DE 10 2026 001 174.4 and is not disclosed publicly.

Compact by design

Height, not footprint.

Where suitable for the application, HEDROTEC's patent-pending architecture can organize selected treatment functions vertically rather than distributing them across a wider plan area — supporting a reduced ground footprint and modular deployment.

  • Integration— multiple treatment functions integrated according to application requirements
  • Footprint— reduced ground area versus an equivalent horizontally arranged process
  • Disclosure— internal geometry confidential pending patent examination
Vertical integration concept, schematic Available hydraulic head above a vertically organized treatment envelope can support head-assisted withdrawal at a lower reference point. The envelope is shown as an abstract outline only, without disclosing internal configuration, treatment sequence, flow direction or component locations. VERTICAL INTEGRATION CONCEPT — SCHEMATIC, NOT TO SCALE AVAILABLE HEAD ΔH INTEGRATED TREATMENT ENVELOPE HEAD-ASSISTED WITHDRAWAL

Conceptual representation only — proprietary internal architecture intentionally undisclosed. Not to scale.


Pillar 06 · digital & AI operations

From process data to predictive operation.

HEDROTEC connects process instrumentation, control logic and AI-assisted models to turn operating data into usable process intelligence — recognizing change in feed-water quality, hydraulic loading, biological behavior, membrane condition and equipment state, and supporting more precise, adaptive operation.

Digital and AI operations concept, schematic Process signals from an instrumented physical treatment system — flow, transmembrane pressure, dissolved oxygen, turbidity and pH among them — feed a central process state model. The model distinguishes a measured trend from a forward-looking predicted trend with a widening uncertainty range, informs an indicative fouling-risk level, and produces bounded operating guidance that returns to the physical process as adaptive parameter response. Illustrative concept only, using representative signals rather than live plant data, and does not disclose internal reactor configuration. PROCESS INTELLIGENCE CONCEPT — ILLUSTRATIVE SIGNALS, NOT LIVE PLANT DATA PHYSICAL PROCESS Instrumented treatment system OBSERVE Process signals FLOW TMP DO TURBIDITY PH PREDICT Process state model NOW MEASURED PREDICTED DEVIATION FOULING RISK — INDICATIVE LOW MODERATE ELEVATED SUPPORT DECISIONS Operating guidance ADJUST AERATION Illustrative recommendation REVIEW BACKWASH INTERVAL CHECK FEED CONDITION Bounded by defined engineering constraints. OPTIMIZE — ADAPTIVE PARAMETER RESPONSE
01
Observe

Process signals

Instrumentation on the physical treatment system provides a continuous picture of operating behavior.

02
Predict

Process state model

Measured trends inform a forward-looking predicted trajectory and an indicative fouling-risk level.

03
Support decisions

Operating guidance

Process signals convert into prioritized, engineering-bounded recommendations.

Illustrative process-intelligence architecture — representative signals, not live plant data or a disclosure of internal reactor configuration.

Predictive monitoring

Surfaces emerging deviations and abnormal trends before threshold alarms alone would provide sufficient context.

Adaptive optimization

Supports adjustment of operating parameters as feed-water characteristics, loading and process response change.

Fouling & cleaning intelligence

Uses membrane and process trends to support condition-based decisions on operation, backwash and cleaning.

Operator decision support

Converts process signals into prioritized diagnostics and operating guidance, bounded by defined engineering constraints.

Engineering principle

Digital intelligence extends process engineering — it does not replace it.

AI-assisted operation remains bounded by hydraulic, biological and membrane constraints, equipment limits, safety logic and the site-specific process design defined during engineering.

Let's talk water

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