Liquid Degasification TRIZ Cases

Single vertical cyclone merges gas-liquid and liquid-solid separation zones to eliminate complex piping while preventing tube plugging.

Segmenting the fixed cone into unit members allows easy installation while a larger sealing member prevents reactant leakage.

Annular main filter element integrates a supplemental filtration layer and coalescer within a single housing.

A solvent regeneration system positions condensed stripper gas return below rich solvent feed to optimize vapor-liquid contacting.

Raised temperature in storage space keeps monomer viscosity low, preventing vacuum path blockages and eliminating frequent cleaning downtime.

A separating device uses projecting tubes to guide gas flow along dividers via the Coanda effect for efficient phase separation.

Upstream gas-liquid separation prevents moisture intake that compromises reliability in wet environments while maintaining cooling airflow.

Centrifugal force separates immiscible fluids in a segmented drum, reducing separation time while maintaining compact volume.

Integrated heating and condensation stages remove diverse contaminants while automated drainage eliminates maintenance needs.

A density-based separator uses inclined rise and descend surfaces to guide laminar flow paths for component separation.

A non-linear level controller maintains liquid levels above a baffle to mitigate slugging effects and prevent equipment damage.

Branched SiOC-linked polyethersiloxanes eliminate hazardous chlorine by-products during synthesis while delivering stable defoaming performance.

A chromatography bubble trap features a permanent opening at its highest point to enable adjustable degassing and excess liquid removal.

A multi-stage ammonia recovery device separates CO2 and H2S from wastewater using pressurized stripping towers.

A gas transfer membrane sequesters carbon dioxide from seawater to remineralize desalinated water with calcium bicarbonate.

A dual-pump system uses a T-fitting separator to divert gas bubbles back to the source, preventing pump gas-binding during sodium hypochlorite injection.

Supercritical water treatment modifies heavy fractions before solvent deasphalting, increasing deasphalted oil yield and extending catalyst life.

A DC bus powers multiple electric machines in a fluid extraction system, allowing each rotor to operate at an independent rotational speed.

A fluid inlet device uses cyclonic separation and guiding vanes to handle high liquid loads in gas-liquid separators.

A humidifying gas apparatus uses a heated liquid duct to evaporate steam that condenses on condensation nuclei.

Replacing threaded flanges with a twist-lock mechanism eliminates bolted mounting requirements while maintaining secure, water-resistant connections.

Demixing the absorbent solution into two phases during regeneration reduces energy consumption by distilling only the acid-enriched fraction.

A stacked separator tank uses pressure control to separate oil and gas from water efficiently.

Ester-terminated polyether additives in polyether siloxane formulations prevent sinkholes and defects while maintaining effective defoaming performance.

A semiconductor device uses segmented fuse data storage and a redundancy signal generator to latch data for memory cell replacement.

Bifurcation openings route liquid into quiet zones where gravity separates particles while buoyancy removes gas, reducing flow resistance.

Segmented thin PTFE tubes break surface tension to move gas bubbles upward, preventing electrical isolation in high pressure reference electrodes.

A cooling apparatus measures generator output, exhaust temperature, and condenser pressure to control spray fluid supply.

Segmented compartments lower fluid velocity and pressure to separate multiphase production fluids into distinct gas, oil, and aqueous phases.

Green rust precipitates remove heavy metals from wastewater without heating, simplifying treatment processes and reducing post-treatment burdens.

Amine and amino acid salt absorbers capture carbon dioxide from gas streams using alkali metal carbonate regeneration to reduce solvent energy demand.

Combined membrane treatment process purifies spherical nickel hydroxide production wastewater through sequential ultrafiltration and reverse osmosis stages.

Inert gas stripping removes volatiles from thermally converted liquids, raising the flash point above 55°C without high energy consumption.

A recycle cup featuring a decreasing section and variable inclination angle separates gas and liquid phases in three-phase reactors.

Segmenting the storage into constant and variable chambers reduces air permeability while enabling effective bubble removal.

A helical flowpath generates centrifugal forces to separate oil droplets from water in multiphase streams.

Helical emulsion preheat coils encircle a dual-chamber firetube to promote initial separation via centrifugal force and heat transfer.

Involute inlet guides process stream into cyclonic chamber to prevent liquid entrainment in gas outlet.

A composite additive system combines a defoaming agent with an air-introducing compound to minimize unwanted air introduction during cement grinding.

An air separator orifice directs fluid upward to stabilize flow and reduce bubble presence at the outlet port.

A one-step separation process recycles natural gas liquids and dry gas from producing wells to support enhanced oil recovery operations.

Preheating make-up water with condensate reduces energy consumption and material costs in steam power plants.

Axial inserts in a reverse flow cyclone prevent transient entrainment of fine particles, reducing filter changes and improving separation capacity.

Segmented inner and outer tubes discharge converted liquid and unconverted gas through independent channels, preventing fluid mixing in tube-in-tube structures.

Co-incinerating amine degradation products in the boiler combustion zone eliminates waste without adding treatment complexity.

Regenerating the absorbing fluid above 3 bar liberates carbon dioxide directly, eliminating costly compression stages for storage.

A fractional-volatilization separator spreads liquid across a frosted quartz interior wall to increase surface area for evaporation.

Sequential curved bends in this separation device minimize turbulence and foaming, reducing cavitation risk in H-Oil reactor pumps.

A naphtha upgrading process separates isoparaffins using an adsorption unit before catalytic conversion to aromatics.

Segmented air separation chambers vent entrained bubbles from dialysate, preventing air embolism risks without adding complex external components.