Fermented Solutions Distillation/Rectification TRIZ Cases

See how a heat pump captures waste heat from distillation vapor and recycles it for process hea

See how an integrated distillation attachment combines heating, stirring, and condensation in o

See how a motor-operated food processor integrates heating, stirring, and distillation with aut

Pure copper tubes and coils adsorb hydrogen sulfide during distillation, reducing burnt off-flavors and improving liquor quality.

Multiple split-and-recombine vapor loops with copper filtration and reflux improve distillation while preserving liquor flavors and aromas.

Removing HCFC-253fb and high boilers before dehydrochlorination cuts 1243zf and vinyl chloride formation, improving 1234yf yield and reactor uptime.

Vapor recompression raises vapor temperature and pressure so latent heat can be reused in distillation and dehydration, cutting steam demand.

UV-A irradiation breaks down sulfur-containing compounds in beverages, improving taste while potentially shortening production time.

Heat from the isopropanol-butanol column condenser drives the butanol column reboiler, cutting extraction energy while preserving separation.

Removing HCFC-253fb before HCFC-244bb dehydrochlorination cuts byproducts, limits reactor coking, and improves 1234yf yield.

A multilayer tower combines staged heating, steam distillation, drying, and cooling to shorten processing and protect heat-sensitive components.

Multiple separation devices remove moisture and concentrate protein, producing animal feed with 45%–64% protein.

Existing NACB processes lose beer-like flavor; staged packed-column separation and water addition preserve ABV without distillation licensing.

Waste-heat reuse across multiple evaporator effects reduces clean steam demand while allowing stillage processing to continue during maintenance.

Selective vacuum removal reduces harsh congeners while retaining ethanol.

A controlled ethanol, ethylene, and ether mixture balances reactor heat to improve propylene yield and limit coke by-products.

Sequential separation devices remove solids and concentrate protein-rich streams, reducing energy costs and greenhouse gas emissions.

A continuous vacuum distillation system processes fermented feed at reduced pressure to preserve flavor integrity.

Vertical dividers segment the pot into independent chambers, enabling parallel flavor production and reducing sequential cooking time.

Cyclic ketones derived from biomass pyrolysis undergo polymerization to form polyketals with improved thermal stability.

Steam stripping removes colored impurities from natural vanillin under an inert atmosphere, achieving high purity and yield without complex equipment.

Replacing liquid acids with solid catalysts and using melt crystallization avoids reactor corrosion while maintaining high yield.

Preliminary distillation reduces impurity load on activated carbon adsorption, increasing removal efficiency for materials causing undesirable colors and odors.

Segmented acidic pretreatment removes nitrogen and sulfur impurities to extend catalyst lifetime.

Exothermic brine absorbs moisture from flue gas to generate heat, preventing condensation corrosion while recovering water through distillation.

Diverting regenerate streams to a feed tank stabilizes distillation and cuts cooling water needs.

A distillation column uses a mechanical compressor to elevate steam pressure and temperature for internal heating.

Deprotonating ethanolamine with a base increases volatility for effective distillation separation.

Aerobic fermentation of post-distillation backset removes inhibitory components, enabling higher recycle rates and fresh water savings.

Denaturing unhydrolyzed cellulose to regenerate surface sites, increasing glucose yield while lowering enzyme costs.

Parallel partition plates enable vapor compression distillation to recover latent heat through gravity flow across alternating evaporation and condensation faces.

Removing cyclic carbonyl compounds and water from biomass-derived 1,4-butanediol via segmented distillation and hydrogenation to improve PBT color tone.

Segmented separator stages and feedback control preserve flavor while removing alcohol, avoiding distillation complexity.

Soxhlet extraction isolates tocopherol from Commiphora myrrha resin, avoiding the potency loss of industrial synthesis.

Engineered microorganisms produce 1,4-butanediol through growth-coupled metabolic pathways, eliminating costly intermediate isolation steps.

Intermittent aeration creates turbulence to wet floating cellulosic particles, enabling high solids concentration saccharification in a single tank.

Engineered microbial biocatalysts produce 1,4-butanediol via exogenous nucleic acids encoding specific biosynthetic enzymes.

Mechanical recompression of combined vapour flows reduces energy consumption in ethanol dewatering, avoiding high costs of traditional distillation.

A pot still heat exchanger uses a mechanical compressor and steam jet pump to recover thermal energy from the cooling water circuit.

Segmented tubular elements create localized heating zones that prevent scorching while reducing fuel consumption during water and spirit purification.

A cooling and phase separation method recovers high-purity 1,3-butadiene and methylethylketone from 2,3-butanediol dehydration products.

Low pressure eductor vapor condenser depressurizes molecular sieves by drawing vapor with a liquid stream to enable continuous ethanol production.

Pre-evaporation of fermented wash reduces mash column load, cutting steam consumption to 1.3 kg per liter.

An air-cooled condenser replaces water-based cooling systems in ethanol distillation to reduce facility water consumption.

Removable copper articles in a stainless steel still reduce sulfur levels while eliminating corrosion and cleaning bottlenecks.

Engineered Escherichia coli organisms produce 1,4-butanediol via exogenous nucleic acids encoding specific biosynthesis enzymes.

A steam eductor mixes waste heat with process liquid to create a heated slurry stream for alcohol production.

A multi-stage process separates 1,4-butanediol using hydrogenation to reduce reactive impurities before final distillation.

Automatic measurement of condensate alcohol content drives a control valve, eliminating manual adjustments and preventing unvaporizable substance contamination.

Rectification of brouillis using an ethanol-water azeotropic mixture separates volatile components from food raw materials.

Reactive distillation converts fermentation-derived alkene precursors into high-purity products, reducing petrochemical costs and environmental impact.

Cascade distillation stages use gaseous methanol streams as heat sources to cut energy consumption and cooling water needs.

GH31 alpha-glucosidase targets resistant bonds in corn fiber, increasing glucose release and ethanol yield without complex processing.