|Exchanger design||Program description||Package||Net price
|Shell-and-tube heat exchangers
||Basic version of design system for shell-and-tube heat exchang-ers for single-phase media (liquid / gaseous) with CAD interface, graphical layout of tubesheet, true-to-scale heat exchanger sketch and interface to LV strength calculation programs. Revised SPIE module.
(see scope of delivery)
|Only as WTS extension|
|1. Pure vapour condensers with desuperheating, condensing and subcooling option, multi-tube, shell without baffles.||KOND||+ 600,--|
|2. Double-pipe heat exchanger (concentric annulus) shell with-out internals.
Thermal and hydraulic design of hairpin heat exchanger incl. modules G2 + GGO + GGLR.
|3. Design of plate fin-and-tube heat exchangers
|Basic version for thermal and hydraulic
design of electrically heated forced-flow shell-and-tube heat exchangers
EWTS as WTS extension
|Vaporization||Vaporization of pure substances at smooth tubes, including tubesheet library, TEMA, incl. essential properties
(see scope of delivery)
|Tube Bundle vibration analysis
- only available in German -
|The calculation may be performed for the complete tube bundle or only for especially endangered zones like tube rows beneath the inlet nozzle or in the window zone.
|Double Pipe heat exchangers
|Heat transfer and pressure loss in double pipe heat exchangers (concentric annulus, tube in tube) see hairpin||DP||1.800,--|
|Crossflow heat exchangers / air coolers
|Cross flow heat exchangers with bare or finned tubes, includes crimped-finned tubes (spiral wound), partial condensation and additional properties (see scope of delivery)||AC||3.100,--|
|Calculation of the intermediate temperatures and quantities of vapour/condensate in vapour/post-vapour condensation in heat exchanger groups (12 types of arrangements)||DNK||1.400,--|
|Multi-component-condenser||Cross flow condensers with bare or finned tubes incl. DDB-Flash (multi-component condensation in the tubes)||MUKO||3.900,--|
|Coil type heat exchangers
|Coil type heat exchangers for gases and liquids. Max. 5 parallel flown-through tubes||COIL||2.300,--|
|Heat transfer and pressure loss in coaxial / coiled double-pipe heat exchangers.||KOAX||1.800,--|
KOAX as COIL Extension
|Thermal oil heaters
|Calculation and simulation of hot oil heaters, includes extensive thermal oil database TOIL
|Coil type economizers for flue gas
|Coil type heat exchangers with up to 14 concentric tube baskets, heating of thermal oil;
Properties of H2O / HFO / Air / OEL / RGAS / TOIL
|Multi-component condensers in German only||Calculation of pure substance / multi-component condensers with / without inert gases (incl. PROPER 3)
|Plate heat exchangers||Pressure drop and heat transfer of chevron-type plates, for single-phase media only, no condensation. Incl. essential properties||MMP||1.400,--|
|Triple tube||Heat exchanger in concentric triple tube||RS3||510,--|
|Hot storage tanks
|Heat losses / heating of storage
TANK calculates the heat losses of insulated and heated stor-age tanks. The floor plan of the tank might be round or rectangular.
> Heat loss by radiation over the roof is considered. Heat loss calculation over the bottom with new mathematical approach. Design of flat heating coil for compensating the heat loss is included.