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PROJECT EVIDENCE

Engineering Case Studies

Compare project scale, feed or process stream, and the membrane sections actually used across tubular membrane engineering, industrial wastewater reuse and ZLD, and process-fluid separation.

All case studies (72)

Showing 1–12 of 30

03 · PROCESS FLUIDS

Process Fluid Membrane Separation

References covering clarification, fractionation, purification, and concentration interfaces for production streams.

Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

15 m³/h Lactic Acid Nanofiltration Purification

Project scale
15 m³/h; linked to a 50,000 t/a production-line record
Feed / process stream
Lactic acid process liquor
Membrane sections
Conditioning/precision filtration + two-stage NF

Separate color bodies, residual sugars, salts, and target product streams through a validated two-stage NF material balance.

The capacity and membrane sections document this reference only; they do not establish design or performance for a new duty.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

2,900 m³/d Allulose Membrane Purification

Project scale
2,900 m³/d
Feed / process stream
Allulose isomerization liquor
Membrane sections
Clarification/protein removal + NF + concentration interface

Connect clarification, fractionation, and concentration sections around the defined sugar profile and downstream product route.

The capacity and membrane sections document this reference only; they do not establish design or performance for a new duty.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

110 m³/h Starch Sugar Clarification

Project scale
110 m³/h
Feed / process stream
Starch sugar saccharification liquor
Membrane sections
Pretreatment + tubular cross-flow clarification

Remove suspended and colloidal material before project-defined refining and concentration operations.

The capacity and membrane sections document this reference only; they do not establish design or performance for a new duty.

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40 m³/h fermentation broth tubular membrane clarification system

Process Fluid Membrane Separation

40 m³/h Fermentation Broth Clarification

Project scale
40 m³/h
Feed / process stream
Fermentation broth
Membrane sections
Conditioning + tubular clarification + downstream purification interface

Separate cells, solids, and suitable macromolecular impurities while defining both clarified and concentrated stream destinations.

The capacity and membrane sections document this reference only; they do not establish design or performance for a new duty.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

50 m³/h Tea Extract Membrane Filtration

Project scale
50 m³/h
Feed / process stream
Aqueous tea extract
Membrane sections
PEK tubular UF clarification + high-pressure RO concentration + spray-drying interface

Clarify an aqueous botanical extract with PEK tubular UF, then concentrate the clarified extract with high-pressure RO before the spray-drying interface.

The capacity and membrane sections document this reference only; they do not establish design or performance for a new duty.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

1,680 m³/d Tubular Membrane Clarification of Saccharified Liquor

Project scale
1,680 m³/d
Feed / process stream
saccharified liquor
Membrane sections
Continuous PEK tubular membrane clarification before further purification

This 1,680 m³/d project processes saccharified liquor. The membrane system continuously separates proteins, colloids, dextrins and other impurities. It replaces the former plate-and-frame filtration step and supplies clarified liquor for further refining.

This reference is for comparison; a new duty requires its own engineering validation.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

55 m³/h Dilute Lactic Acid Membrane Concentration

Project scale
55 m³/h
Feed / process stream
dilute lactic acid liquor
Membrane sections
High-pressure membrane concentration + permeate reuse + evaporation interface

This 55 m³/h project processes dilute lactic acid liquor. The membrane stage recovers and concentrates dilute lactic acid. Permeate is reused and concentrate proceeds to evaporation. This case and the 15 m³/h lactic-acid NF case document different sections at the same plant.

This reference is for comparison; a new duty requires its own engineering validation.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

40 m³/h Lactic Acid Condensate Recovery and Concentration

Project scale
40 m³/h
Feed / process stream
dilute lactic acid liquor in evaporation condensate
Membrane sections
High-pressure membrane recovery and concentration + permeate reuse + evaporation interface

This 40 m³/h project processes dilute lactic acid liquor in evaporation condensate. The membrane stage recovers dilute lactic acid from evaporation condensate. Permeate returns to process-water reuse and concentrate proceeds to evaporation. This case and the 20 m³/h lactic-acid NF case cover different sections at the same plant.

This reference is for comparison; a new duty requires its own engineering validation.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

300 m³/d ABA Fermentation Broth Membrane Separation

Project scale
300 m³/d
Feed / process stream
ABA fermentation broth
Membrane sections
PEK tubular membrane separation + UF purification + high-pressure RO concentration

This 300 m³/d project processes ABA fermentation broth. The membrane stages provide broth clarification, purification and concentration as an integrated membrane processing system for the ABA stream.

This reference is for comparison; a new duty requires its own engineering validation.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

6 m³/h Cistanche Extract Membrane Processing

Project scale
6 m³/h
Feed / process stream
Cistanche extract
Membrane sections
Tubular UF clarification + NF concentration + column-treatment interface + RO alcohol removal and concentration of the eluate

This 6 m³/h project processes Cistanche extract. Tubular UF removes proteins, pectin and starch. NF concentrate feeds the column-treatment stage, while a separate RO stage removes alcohol and concentrates the column eluate.

This reference is for comparison; a new duty requires its own engineering validation.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

120 m³/h Soy Sauce Ultrafiltration Clarification

Project scale
120 m³/h
Feed / process stream
soy sauce
Membrane sections
Ultrafiltration clarification with microbial and impurity separation

This 120 m³/h project processes soy sauce. Ultrafiltration clarifies soy sauce and provides impurity separation and microbial control using hygienic membrane equipment. This case documents the soy-sauce project.

This reference is for comparison; a new duty requires its own engineering validation.

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Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

300 m³/d Integrated Membranes for BCAA Fermentation Broth

Project scale
300 m³/d
Feed / process stream
leucine, isoleucine and valine fermentation broth
Membrane sections
PEK tubular UF clarification + NF decolorization and purification + RO concentration

This 300 m³/d project processes leucine, isoleucine and valine fermentation broth. Tubular UF separates cells, proteins and polysaccharides. NF provides decolorization and purification, and RO concentrates the stream before downstream ion exchange and crystallization.

This reference is for comparison; a new duty requires its own engineering validation.

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PROJECT CONTEXT

Use references for comparison, not as a new-project guarantee