Open menu

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 49–60 of 72

All case studies

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.

View case details →
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.

View case details →
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.

View case details →
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.

View case details →
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.

View case details →
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.

View case details →
Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

2,500 m³/d Glucose Liquor Tubular Membrane Clarification

Project scale
2,500 m³/d
Feed / process stream
saccharified glucose liquor
Membrane sections
Continuous PEK tubular clarification + downstream ion-exchange interface

This 2,500 m³/d project processes saccharified glucose liquor. Tubular membranes separate proteins, colloids, dextrins and other impurities. The system performs the clarification duty previously handled by plate-and-frame filtration, ahead of ion exchange and further refining.

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

View case details →
Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

13 m³/h L-Lactic Acid Nanofiltration Purification

Project scale
13 m³/h
Feed / process stream
lactic acid liquor
Membrane sections
Two-stage NF for decolorization and residual-sugar separation

This 13 m³/h project processes lactic acid liquor. Two-stage nanofiltration decolorizes the lactic acid liquor and separates residual sugars, preparing purified liquor for downstream evaporation and concentration.

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

View case details →
Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

20 m³/h L-Lactic Acid Nanofiltration Purification

Project scale
20 m³/h
Feed / process stream
lactic acid production liquor
Membrane sections
Two-stage NF for decolorization and residual-sugar separation

This 20 m³/h project processes lactic acid production liquor. The system serves a 100,000 t/a lactic acid production line. Two-stage NF decolorizes the liquor and separates residual sugars before evaporation. The 40 m³/h dilute-lactic-acid recovery case covers a different section at the same plant.

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

View case details →
Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

120 m³/h Fructose Liquor Tubular Membrane Clarification

Project scale
120 m³/h
Feed / process stream
fructose liquor
Membrane sections
PEK tubular clarification + downstream refining interface

This 120 m³/h project processes fructose liquor. Tubular membranes separate suspended solids and macromolecular impurities from fructose liquor, providing clarified feed for downstream sugar refining.

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

View case details →
Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

20 m³/h L-Arabinose Broth Tubular Membrane Clarification

Project scale
20 m³/h
Feed / process stream
L-arabinose fermentation broth
Membrane sections
PEK tubular clarification + downstream chromatography interface

This 20 m³/h project processes L-arabinose fermentation broth. Tubular membranes separate cells, proteins, impurities and part of the color bodies, providing pretreatment before downstream chromatographic separation and refining of L-arabinose.

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

View case details →
Membrane equipment at a process-fluid separation project

Process Fluid Membrane Separation

3 m³/h Jujube and Pomegranate Wine Membrane Clarification

Project scale
3 m³/h
Feed / process stream
jujube wine and pomegranate wine
Membrane sections
PEK tubular ultrafiltration clarification

This 3 m³/h project processes jujube wine and pomegranate wine. Ultrafiltration separates suspended impurities from jujube and pomegranate wines to provide clarified liquor.

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

View case details →

PROJECT CONTEXT

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