Fluid mixture separation by low temperature glide heat

Power plants – Motive fluid energized by externally applied heat – Power system involving change of state

Reexamination Certificate

Rate now

  [ 0.00 ] – not rated yet Voters 0   Comments 0

Details

C060S649000, C060S653000, C060S673000, C062S114000, C062S476000, C062S495000, C202S158000, C202S159000

Reexamination Certificate

active

06715290

ABSTRACT:

REFERENCE TO A MICROFICHE APPENDIX
Not applicable
BACKGROUND OF THE INVENTION
There is an increasing need to extract beneficial effect (e.g., power and/or refrigeration) from low temperature heat, which is frequently regarded as waste heat. Heat-activated absorption cycles provide exceptional promise in this regard.
Many low temperature heat sources have a temperature glide—the more heat that is extracted, the lower the temperature becomes. All sensible heat sources have that characteristic, e.g., exhaust combustion gas from an engine or furnace, hot process liquids, or geothermal liquid. Pure component latent heat (e.g., saturated steam) is isothermal, but mixed component condensation has a glide. Solar radiation may be regarded as isothermal, but once it is captured in a heat transfer fluid it has a glide.
In order to extract maximum useful effect from a glide heat source, the application process needs to accomplish two equally important objectives: the heat acceptance should have a glide comparable to that of the source, and it should reduce the source temperature a maximal amount. These two considerations respectively denote the quality and the quantity of heat input.
In principle absorption cycles excel at those two objectives, since they are thermodynamically capable of accepting heat input with temperature glide, and also of being powered by heat down to very low temperatures, e.g., less than 100° C.
However, the prior art practice in heat-activated absorption cycles does not make full use of this capability. Flame powering or steam powering has no need for it—all the heat is input at the hottest end of the hottest component of the cycle—the generator. In volatile absorbent cycles, that component is also known as the reboiler.
Prior art examples of inputting heat to absorption cycles are found in U.S. Pat. Nos. 3,690,121; 4,307,572; 6,357,255; and International Publication WO 01/94757.
With a volatile absorbent, the process of desorbing the sorbate vapor from the sorbent liquid is effectively distillation. When heat is referred to as “low temperature,” it signifies that at least part of it is at a temperature below the peak distillation or de sorption temperature.
In its broadest aspect, this invention discloses the distillation of a fluid mixture using low temperature glide heat. Distillation is generically useful in many applications, and this disclosure allows it to be accomplished with lower temperature heat than heretofore possible. The particular focus of this disclosure is on distillation incorporated in an absorption cycle with a volatile absorbent, and with useful effect either chilling or power.
Thus included among the objects of this invention is to achieve more beneficial distillation effect from a given low temperature glide heat source than has heretofore been possible, and in the context of an absorption cycle, to achieve more refrigeration and/or power from that source than heretofore possible.
BRIEF SUMMARY OF THE INVENTION
The above and additional useful objects are obtained by an apparatus for distilling a fluid mixture using low temperature heat comprised of:
a) a distillation column;
b) a heat recovery vapor generator (HRVG);
c) a splitter for the fluid mixture, which directs a minor fraction to the upper reflux portion of the distillation column, and the remainder to the heat recovery vapor generator;
d) a flowpath for two-phase fluid from the HRVG to the lower portion of the distillation column; and
e) a heat exchanger in the central portion of said column which is supplied column bottom liquid.
Related variants of this disclosure extend to various sensible heat recuperation schemes between column fluids, and to the use of more than one heat recovery vapor generator in series, as described further below.


REFERENCES:
patent: 3690121 (1972-09-01), Patel
patent: 4307572 (1981-12-01), Brinkerhoff
patent: 4418545 (1983-12-01), Markfort
patent: 4707996 (1987-11-01), Vobach
patent: 4724679 (1988-02-01), Radermacher
patent: 4962646 (1990-10-01), Rathbone
patent: 5186012 (1993-02-01), Czachorski et al.
patent: 5916258 (1999-06-01), Cho
patent: 6269644 (2001-08-01), Erickson et al.
patent: 6357255 (2002-03-01), Onishi et al.
patent: 6517801 (2003-02-01), Watson et al.
Jurgen Langren, “Cogen Absorption Plants for refrigeration purposes and turbine air inlet cooling”, Cogeneration On Site Power Production, Mar.-Apr. 2002, pp. 46-49.
Werner F. Malewski, Gunther M. Holldorff, “Power Increase of Gas Turbines by Inlet Air Pre-Cooling with Absorption Refrigeration Utilizing Exhaust Waste heat”, ASME #86-GT-67, New York, NY 1986.

LandOfFree

Say what you really think

Search LandOfFree.com for the USA inventors and patents. Rate them and share your experience with other people.

Rating

Fluid mixture separation by low temperature glide heat does not yet have a rating. At this time, there are no reviews or comments for this patent.

If you have personal experience with Fluid mixture separation by low temperature glide heat, we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and Fluid mixture separation by low temperature glide heat will most certainly appreciate the feedback.

Rate now

     

Profile ID: LFUS-PAI-O-3218129

  Search
All data on this website is collected from public sources. Our data reflects the most accurate information available at the time of publication.