FIELD: tubular heat exchangers, boiler units for shipbuilding, metallurgy, power engineering and chemical industry.
SUBSTANCE: proposed heat exchange pipe has spherical recesses directed inside and located in staggered order on outer surface; pipe is made at the following geometric relationships:  =0.035-0.175;
=0.035-0.175;  =0.35-0.70; n=1-5, where h is depth of spherical recesses, mm; t is pitch of spherical recesses along pipe axis, mm; n is number of recesses in cross section;
=0.35-0.70; n=1-5, where h is depth of spherical recesses, mm; t is pitch of spherical recesses along pipe axis, mm; n is number of recesses in cross section;  is outer diameter of initial smooth pipe, mm.
 is outer diameter of initial smooth pipe, mm.
EFFECT: intensification of heat exchange.
8 dwg, 1 tbl
| Title | Year | Author | Number | 
|---|---|---|---|
| HEAT EXCHANGE TUBE MANUFACTURING METHOD | 2009 | 
 | RU2382974C1 | 
| CONDENSER HEAT-EXCHANGE PIPE | 0 | 
 | SU1071068A1 | 
| HEAT-EXCHANGE SURFACE | 2001 | 
 | RU2200926C2 | 
| HEAT EXCHANGE TUBE | 0 | 
 | SU1746196A1 | 
| HEATING ELEMENT | 1993 | 
 | RU2027968C1 | 
| SHELL-AND-TUBE HEAT EXCHANGER | 2019 | 
 | RU2734614C1 | 
| HEAT EXCHANGING SURFACE | 2016 | 
 | RU2610636C1 | 
| HEAT-EXCHANGE ELEMENT | 1993 | 
 | RU2033592C1 | 
| METHOD FOR SAMPLING MULTIPHASE LIQUID FROM A PIPELINE AND A DEVICE FOR SAMPLING MULTIPHASE LIQUID FROM A PIPELINE | 2020 | 
 | RU2755939C1 | 
| SHELL-AND-TUBE HEAT EXCHANGER | 2011 | 
 | RU2489664C1 | 
Authors
Dates
2004-06-20—Published
2002-07-22—Filed