Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
172 words
A corrugated core structure for a heat exchanger, said core structure comprising: a plate having parallel rows of corrugations, the walls of the corrugations defining passages for streams of a heat-transfer agent to flow therethrough, pairs of opposed projections and recesses successively separated by smooth wall portions, the pairs of projections and recesses being arranged in opposition to one another so as to form divergent-convergent portions of the passages and having a length sufficient to intensify the heat transfer process; the smooth portions of the passages alternating with said divergent-convergent portions such that, in combination, they provide for successive throttling of the flow of the heat-transfer agent to intensify the heat transfer process, each said smooth portion of the passage having a length essentially below five values of the hydraulic diameter of said smooth portion in the passage; the vertices of said corrugations being bent on a radius, the value of which is essentially below a difference between one fourth of the pitch of said corrugations and one-half the wall thickness thereof.
Claim 2
Dependent Claim
172 words
A corrugated core structure for a heat exchanger, said core structure comprising: a plate having parallel rows of corrugations, the walls of the corrugations defining passages for streams of a heat-transfer agent to flow therethrough, pairs of opposed projections and recesses successively separated by smooth wall portions, the pairs of projections and recesses being arranged in opposition to one another so as to form divergent-convergent portions of the passages and having a length sufficient to intensify the heat transfer process; the smooth portions of the passages alternating with said divergent-convergent portions such that, in combination, they provide for successive throttling of the flow of the heat-transfer agent to intensify the heat transfer process, each said smooth portion of the passage having a length essentially below five values of the hydraulic diameter of said smooth portion in the passage; the vertices of said corrugations being bent on a radius, the value of which is essentially below a difference between one fourth of the pitch of said corrugations and one-half the wall thickness thereof.
Claim 3
Dependent Claim
65 words
A corrugated core structure as claimed in claim 1, wherein the projections and recesses are of a length n, or ##EQU5## where F is open area of the smooth portion of the passage; d * is given hydraulic diameter of the narrowest cross-section in the passage; d is given hydraulic diameter of the smooth portion of the passage; and m is height of the projections.
Claim 4
Dependent Claim
140 words
A heat exchange element having a corrugated surface formed from a plate having parallel rows of corrugations wherein the corrugation walls define passages for the flow of a heat exchange agent, said corrugated walls having projections and recesses successively separated by smooth wall portions and spaced in an opposed relationship on adjacent corrugated walls to form converging and diverging passages in order to effect periodic throttling of the heat exchange agent and thereby intensify the heat exchange process, wherein each smooth portion of said passages has a length ranging from nil to five flow diameters at the smooth portion of the passage, and wherein the inside radius of the corrugation crest is less than the difference between one-fourth of the corrugation pitch and one-half its wall thickness and is equal to 35 to 95% of the value of the radius.
Claim 5
Dependent Claim
140 words
A heat exchange element having a corrugated surface formed from a plate having parallel rows of corrugations wherein the corrugation walls define passages for the flow of a heat exchange agent, said corrugated walls having projections and recesses successively separated by smooth wall portions and spaced in an opposed relationship on adjacent corrugated walls to form converging and diverging passages in order to effect periodic throttling of the heat exchange agent and thereby intensify the heat exchange process, wherein each smooth portion of said passages has a length ranging from nil to five flow diameters at the smooth portion of the passage, and wherein the inside radius of the corrugation crest is less than the difference between one-fourth of the corrugation pitch and one-half its wall thickness and is equal to 35 to 95% of the value of the radius.