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.
Showing 61–72 of 72
All case studies
Process Fluid Membrane Separation
3 m³/d Iron Dextran Nanofiltration Purification and Concentration
This 3 m³/d project processes iron dextran solution. Nanofiltration purifies and concentrates the iron dextran solution while separating sodium chloride impurities as a membrane stage in the refining process.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
10 m³/d Nucleoside and Nucleotide Membrane Separation
This 10 m³/d project processes nucleoside and nucleotide fermentation liquor. The UF and NF stages provide separation and concentration for nucleoside and nucleotide fermentation liquor before subsequent extraction and refining.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
50 m³/h Dilute Polyol Liquor Membrane Concentration
This 50 m³/h project processes dilute polyol liquor. High-pressure membranes preconcentrate the dilute polyol liquor. Permeate is reused and concentrate proceeds to downstream evaporation and refining.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
20 m³/h Glucose–Fructose Syrup Nanofiltration Purification
This 20 m³/h project processes glucose–fructose syrup. Nanofiltration fractionates and purifies the syrup by separating polysaccharides and other oligosaccharide impurities before further product refining.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
10 m³/h Baicalin Extract Membrane Separation
This 10 m³/h project processes baicalin extract. Tubular membranes separate solids and colloids before downstream protein removal and concentration. Plum supplied all membrane-stage equipment for this project.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
20 m³/d Andrographis Extract Membrane Separation
This 20 m³/d project processes Andrographis extract. Tubular membranes separate suspended solids, colloids and macromolecular impurities. The nanofiltration stage provides alcohol removal and extract concentration.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
40 m³/h Integrated Membrane Processing for Inulin Extract
This 40 m³/h project processes chicory and Jerusalem artichoke extracts. Tubular UF clarifies the extract. NF separates salts and monosaccharides while concentrating inulin; a separate high-pressure RO stage concentrates the monosaccharide branch.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
400 m³/d Integrated Membrane Processing for Xylo-Oligosaccharides
This 400 m³/d project processes enzymatic extract from steam-exploded corn cobs. The membrane system supports xylo-oligosaccharide production. Tubular UF removes proteins, starch and pectin; other stages provide NF desalting and monosaccharide separation, UF decolorization and high-pressure RO concentration of the monosaccharide stream.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
2,400 m³/d Tubular Membrane Clarification for Xylo-Oligosaccharides
This 2,400 m³/d project processes xylo-oligosaccharide extract obtained by enzymatic treatment of corn stalks. This case covers tubular membrane clarification of the extract before downstream UF, NF and refining. The recorded equipment scope for this case is the PEK tubular membrane system.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
100 m³/d p-Hydroxyphenylglycine Membrane Purification
This 100 m³/d project processes p-hydroxyphenylglycine process liquor. Tubular UF separates cells, proteins and other impurities. Downstream NF provides decolorization and purification before further refining.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
500 m³/d Sodium Gulonate Fermentation Broth Clarification
This 500 m³/d project processes sodium gulonate fermentation broth from vitamin C production. Tubular membranes separate cells, suspended solids and macromolecular proteins, providing clarified liquor for the subsequent purification stages.
This reference is for comparison; a new duty requires its own engineering validation.
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Process Fluid Membrane Separation
1,300 m³/d L-Alanine Fermentation Broth Membrane Purification
This 1,300 m³/d project processes L-alanine fermentation broth. Tubular UF separates cells and macromolecular impurities. NF then provides decolorization and purification before downstream evaporation and crystallization.
This reference is for comparison; a new duty requires its own engineering validation.
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