US3802186A - Generation of power using a rankine-cycle engine with tetrachloroethylene as the working fluid - Google Patents

Generation of power using a rankine-cycle engine with tetrachloroethylene as the working fluid Download PDF

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US3802186A
US3802186A US00269380A US26938072A US3802186A US 3802186 A US3802186 A US 3802186A US 00269380 A US00269380 A US 00269380A US 26938072 A US26938072 A US 26938072A US 3802186 A US3802186 A US 3802186A
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tetrachloroethylene
rankine
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power
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W Mahler
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EIDP Inc
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EI Du Pont de Nemours and Co
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01KSTEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K25/00Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
    • F01K25/08Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours

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  • ABSTRACT Tetrachloroethylene has excellent physical properties as the working fluid in a Rankine-cycle engine. Thermal degradation of the working fluid can be reduced to acceptable levels by contacting the fluid with at least ten sq. cm of ferritic iron per cc of tetrachloroethylene when at temperatures greater than 200C.
  • Small engines adapted for portability should preferably employ a single stage impulse turbine. This requires the use of working fluids having a higher molecular weight in order to reduce the efflux velocity at the nozzle and the speed of the turbine for a single stage. It is also highly desirable to operate below the critical temperature of the liquid in order to minimize the pressure requirements.
  • 3,516,248 has taught the use of a variety of non-halogenated organic fluids having the property that the change in entropy from the maximum saturated enthalpy point on 21 M01- lier diagram to the entropy of the saturated vapor at atmospheric pressure is less than 0.1 BTU/(F).
  • Tetrachloroethylene has also been proposed as a working fluid for Rankine-cycle engines by Paxton U.S. Pat. No. 3,512,357. Although tetrachloroethylene has desirable thermal properties and is relatively inexpensive, the thennal stability at elevated temperatures needed for Rankine-cycle engines is inadequate.
  • the present invention is directed to a method of generating power wherein tetrachloroethylene is vaporized at a temperature greater than 200C, the vapor is expanded and does work, and is thereafter condensed and recycled, wherein the tetrachloroethylene is stabilized in the liquid phase by contacting the liquid with ferritic iron in an amount sufficient to provide a surface of ferritic metal/volume of liquid tetrachloroethylene of at least 10 cm".
  • ferrous metal refers to metals or alloys in which metallic iron is the major component such as 1020 steel, 1018 steel, 303 stainless steel and the like. While stainless steel suffers the least corrosion and does effect some degree of stabilization, best results are obtained with ferritic steels such as 1018 steel or ordinary iron.
  • the amount required to achieve significant stabilization should provide at least 10 sq cm of surface per cubic centimeter of liquid tetrachloroethylene and should be in contact with the liquid. This amount is greater than is found in conventional boilers. For example, a tube-type boiler with tubes having an inside diameter of 0.5 inches provides surface/volume ratio of 3:1 cm. Accordingly, it is preferred to pack the boiler with steel wool or to employ iron metal grids or fine iron metal powder to achieve the desired stabilization.
  • Table I shows the results of tests wherein 1018 cold rolled steel, 430 stainless steel (17% Cr) and Pl 1 steel (a low alloy steel containing 1.3% Cr and 0.5% Mo) are heated to 300C for 28 days in sealed glass tubes with tetrachloroethylene.
  • FIG. 1 shows the entropy-temperature diagram which has been determined for tetrachloroethylene.
  • FIG. 2 is a schematic view of a turbine power generator adapted for use with tetrachloroethylene as a working substance.
  • the critical temperature of tetrachloroethylene is 662.9F and the critical pressure is 568.75 psia.
  • the value of ds/dT for the saturated vapor line is very slightly positive, i.e., the change in entropy in passing from the critical temperature to the boiling point is less than 0.02 BTU/(lb.F). Accordingly, vapor produced by expansion of saturated vapor from a temperature below the critical temperature to the pressure of the condenser will be only slightly superheated so that an efficient Rankine-cycle engine can be operated without the problems encountered with vapor/liquid mixtures after expansion, e.g., at the turbine wheel, while the degree of superheat after expansion is so slight that it can be neglected. Thus, regenerative cooling of the vapor prior to condensation is unnecessary.
  • FIG. 1 A typical cycle employed in Rankine cycle engines is shown in FIG. 1.
  • the vapor is produced essentially saturated at a temperature of 475F corresponding to point 1 of FIG. 1 at a pressure of 178.4 psia.
  • the gas is expanded essentially isentropically to a pressure of 3 psia, the condenser pressure, and cooling to a temperature of 205F indicated by point 2 in FIG. 1 whereupon the gas does work in, for example, a turbine.
  • the gas is then cooled to 160F (3) and condensed to a liquid at 160F (4) in the condenser.
  • the condensed liquid is pumped back to the boiler and heated to 475F (5) at which temperature the liquid is vaporized to vapor at 475F and 178.4 psia, thus completing the cycle.
  • the Rankine cycle efficiency is 26.6%.
  • the small amount of superheat can be recovered by a heat exchanger or regenerator and employed to heat the boiler feed.
  • 70% regeneration the efficiency is only increased to 27.4
  • FIG. 2 is a schematic diagram of a turbine engine operating on the cycle described above in connection with FIG. 1 using tetrachloroethylene as the working fluid.
  • the vapor is expanded in the nozzles of turbine 11 and cooled, the expanded vapor doing work on the blades of the turbine.
  • the vapor at about 205F is transferred to the condenser 12, cooled and condensed and the liquid pumped back to the boiler 10 by pump 13.
  • tetrachloroethylene has other desirable properties.
  • the molecular weight of tetrachloroethylene is 166.
  • Tetrachloroethylene liquid has a density of 1.6l at 25C and is well suited for use in such high density, low weight equipment. Flammability Tetrachloroethylene is not flammable and therefore presents no fire or explosion hazard, in the event of damage to the heated engine.
  • Tetrachloroethylene has low toxicity: inhalation of the vapor at a concentration of ppm per 8 hour day is permissible. Tetrachloroethylene is not considered a contributory cause of smog.

Abstract

Tetrachloroethylene has excellent physical properties as the working fluid in a Rankine-cycle engine. Thermal degradation of the working fluid can be reduced to acceptable levels by contacting the fluid with at least ten sq. cm of ferritic iron per cc of tetrachloroethylene when at temperatures greater than 200*C.

Description

United States Patent 1191 Mahler Apr. 9, 1974 [541 GENERATION OF POWER USING A 3,512,357 5/1970 Paxton 60/36 RANKINE CYCLE ENGINE WITH 3,527,703 9/1970 Archer 260/6525 R TETRACHLOROETHYL N AS THE FOREIGN PATENTS OR APPLICATIONS WORKING FLUID 526,733 7/1921 France 60/36 [75] Inventor: Walter Mahler, Wilmington, Del.
[73] Assignee: E. l. du Pont de Nemours and Company, Wilmington, Del.
[22] Filed: July 6, 1972 [21 Appl. No.: 269,380
Related US. Application Data [63] Continuation-impart of Ser. No. 68,740, Sept. 1,
I970, abandoned.
[52] 11.5. CI. ..60/649, 252/400 R {51] Int. Cl. F0lk 25/00, F0lk 3/18 [58] Field of Search 60/36, 38; 252/67, 400 R; 260/6525 [56] References Cited UNITED STATES PATENTS 2,371,644 3/1945 Petering 260/6525 R 3,237,403 3/1966 Feher 60/36 PUMP OTHER PUBLICATlONS The Condensed Chemical Dictionary, 6th Edition, by Arthur Rose et a1., Reinhold Publishing Corp; N.Y. (Definition of Perchloroethylene, Page No. (Unknown) Fifth Edition dated 1965.
Primary ExaminerEdgar W. Geoghegan Assistant ExaminerH. Burks, Sr.
[ 5 7 ABSTRACT Tetrachloroethylene has excellent physical properties as the working fluid in a Rankine-cycle engine. Thermal degradation of the working fluid can be reduced to acceptable levels by contacting the fluid with at least ten sq. cm of ferritic iron per cc of tetrachloroethylene when at temperatures greater than 200C.
1 Claim, 2 Drawing Figures WEB/NE CONQEMSER GENERATION OF POWER USING A RANKINE-CYCLE ENGINE WITH TETRACIILOROETHYLENE AS THE WORKING FLUID RELATED APPLICATIONS This application is a continuation-in-part of U.S. Ser. No. 68,740, filed Sept. 1, 1970, now abandoned.
BACKGROUND OF THE INVENTION Rankine cycle, high power, multistage, vapor turbines are well known as highly efficient heat engines for the production of power. When steam is employed, it is essential to employ multiple stages to obtain power at usable speeds and at useful efficiency. Superheat is also required, since, on expansion, saturated steam forms a mixture of vapor and liquid water which erodes turbine blades and is difficult to handle. Accordingly, steam turbines are generally complex pieces of equipment which are ill adapted to manufacture and operate on the small scale needed for portable engines of modest power, i.e., less than 1,000 hp.
Small engines adapted for portability should preferably employ a single stage impulse turbine. This requires the use of working fluids having a higher molecular weight in order to reduce the efflux velocity at the nozzle and the speed of the turbine for a single stage. It is also highly desirable to operate below the critical temperature of the liquid in order to minimize the pressure requirements.
Many organic liquids have been proposed for use as working fluids for engines. For example, Fulton U.S. Pat. No. 795,761 has suggested such fluids as alcohol, ether, carbon disulfide or chloroformas working fluids. Govers U.S. Pat. No. 870,507 teaches the use of chlorides of carbon such as carbon tetrachloride, chloroform, ethylidene chloride or trichloroethane. Norton et al. U.S. Pat. No. 3,511,049 and Minto U.S. Pat. No. 3,479,817 have taught the use of chlorofluorohydrocarbons, and McEwan U.S. Pat. No. 3,516,248 has taught the use of a variety of non-halogenated organic fluids having the property that the change in entropy from the maximum saturated enthalpy point on 21 M01- lier diagram to the entropy of the saturated vapor at atmospheric pressure is less than 0.1 BTU/(F).
Tetrachloroethylene has also been proposed as a working fluid for Rankine-cycle engines by Paxton U.S. Pat. No. 3,512,357. Although tetrachloroethylene has desirable thermal properties and is relatively inexpensive, the thennal stability at elevated temperatures needed for Rankine-cycle engines is inadequate.
SUMMARY OF THE INVENTION The present invention is directed to a method of generating power wherein tetrachloroethylene is vaporized at a temperature greater than 200C, the vapor is expanded and does work, and is thereafter condensed and recycled, wherein the tetrachloroethylene is stabilized in the liquid phase by contacting the liquid with ferritic iron in an amount sufficient to provide a surface of ferritic metal/volume of liquid tetrachloroethylene of at least 10 cm".
THE DRAWINGS AND DETAILED DESCRIPTION OF THE INVENTION It has long been known that tetrachloroethylene has relatively low stability. Stabilizers suitable for stabilizing this compound have been described in many patents including U.S. Pat. Nos. 2,492,048; 2,997,507; 2,947,792; 2,094,367 and 2,096,735. While such stabilizers are effective for moderate temperatures such as those employed in dry cleaning, they are not effective in preventing the degradation of tetrachloroethylene at higher temperatures such as 246C (475F) employed in external combustion engines, even in sealed systems. Surprisingly, it has been found that the degradation of tetrachloroethylene can be inhibited by the presence of ferrous metals in the system. The term ferrous metal refers to metals or alloys in which metallic iron is the major component such as 1020 steel, 1018 steel, 303 stainless steel and the like. While stainless steel suffers the least corrosion and does effect some degree of stabilization, best results are obtained with ferritic steels such as 1018 steel or ordinary iron. The amount required to achieve significant stabilization should provide at least 10 sq cm of surface per cubic centimeter of liquid tetrachloroethylene and should be in contact with the liquid. This amount is greater than is found in conventional boilers. For example, a tube-type boiler with tubes having an inside diameter of 0.5 inches provides surface/volume ratio of 3:1 cm. Accordingly, it is preferred to pack the boiler with steel wool or to employ iron metal grids or fine iron metal powder to achieve the desired stabilization.
Table I shows the results of tests wherein 1018 cold rolled steel, 430 stainless steel (17% Cr) and Pl 1 steel (a low alloy steel containing 1.3% Cr and 0.5% Mo) are heated to 300C for 28 days in sealed glass tubes with tetrachloroethylene.
TABLE I Decomposition of Tetrachloroethylene and Corrosion in the Presence of Ferrous Metals: 28 days at 300C 1018 Steel Corrosion Other Corrosion C Cl S/V cm" Mg/cm S/V cm Mg/cm after test 0.8 260 0 1.5 129 0 3.0 33 14.7 6.0 11 23.8
In another experiment 0.3 gm of iron powder having an estimated surface area of 700 cm was combined with 0.3 cc. of tetrachloroethylene in a 2 cc tube and heated for 28 days at 300C. At the end of this period the tetrachloroethylene was analyzed by gas chromatography and found to be 99.1% pure.
The reason for the stabilizing action of iron is not known and it is possible that a compound derived from iron such as FeCl rather than the metal itself is the effective stabilizer.
In the accompanying drawings:
FIG. 1 shows the entropy-temperature diagram which has been determined for tetrachloroethylene.
FIG. 2 is a schematic view of a turbine power generator adapted for use with tetrachloroethylene as a working substance.
Referring now to FIG. 1, the critical temperature of tetrachloroethylene is 662.9F and the critical pressure is 568.75 psia. The value of ds/dT for the saturated vapor line is very slightly positive, i.e., the change in entropy in passing from the critical temperature to the boiling point is less than 0.02 BTU/(lb.F). Accordingly, vapor produced by expansion of saturated vapor from a temperature below the critical temperature to the pressure of the condenser will be only slightly superheated so that an efficient Rankine-cycle engine can be operated without the problems encountered with vapor/liquid mixtures after expansion, e.g., at the turbine wheel, while the degree of superheat after expansion is so slight that it can be neglected. Thus, regenerative cooling of the vapor prior to condensation is unnecessary.
A typical cycle employed in Rankine cycle engines is shown in FIG. 1. The vapor is produced essentially saturated at a temperature of 475F corresponding to point 1 of FIG. 1 at a pressure of 178.4 psia. The gas is expanded essentially isentropically to a pressure of 3 psia, the condenser pressure, and cooling to a temperature of 205F indicated by point 2 in FIG. 1 whereupon the gas does work in, for example, a turbine. The gas is then cooled to 160F (3) and condensed to a liquid at 160F (4) in the condenser. The condensed liquid is pumped back to the boiler and heated to 475F (5) at which temperature the liquid is vaporized to vapor at 475F and 178.4 psia, thus completing the cycle. With the above cycle, the Rankine cycle efficiency is 26.6%. The small amount of superheat can be recovered by a heat exchanger or regenerator and employed to heat the boiler feed. However, with 70% regeneration, the efficiency is only increased to 27.4
FIG. 2 is a schematic diagram of a turbine engine operating on the cycle described above in connection with FIG. 1 using tetrachloroethylene as the working fluid. The boiler indicated by heats the liquid and vaporizes it to saturated vapor. The vapor is expanded in the nozzles of turbine 11 and cooled, the expanded vapor doing work on the blades of the turbine. The vapor at about 205F is transferred to the condenser 12, cooled and condensed and the liquid pumped back to the boiler 10 by pump 13. In addition to the substantial efficiency which can be obtained in a Rankine cycle engine as described above, tetrachloroethylene has other desirable properties.
Molecular Weight The molecular weight of tetrachloroethylene is 166.
Since the efflux velocity on expansion in a nozzle is roughly in inverse proportion to the square root of the molecular weight, sufficiently low efflux velocities can be achieved to render a single stage impulse turbine feasible. The low efflux velocities and the relatively low operating temperatures make the use of light metals such as aluminum or even plastics feasible for construction of the turbine blades.
Melting Point and Boiling Point The melting point of tetrachloroethylene of l9C (0F) makes the use of the liquid as a working fluid feasible even when relatively low ambient temperatures are encountered. The boiling point of 121C (250F) provides reasonably efficient condensing with gaseous or liquid coolants at ambient temperatures.
Liquid Density In the copending commonly assigned applications of William A. Doemer, U.S. Ser. No. 110,478 filed Jan. 28, 1971 as a continuation-in-part of US. Ser. No. 25,857 filed Apr. 6, 1970 and now abandoned, U.S. Ser. No. 231,232 filed Mar. 2, 1972 and US. Ser. No. 227,902 filed Feb. 22, 1972; also US. Pat Nos. 3,590,786 and 3,613,638 to William A. Doerner there are disclosed rotary engines, rotary boilers and rotary regenerators for low-pressure application. In the case of the rotary boilers and regenerators, high density liquids are particularly desirable to minimize the speed of rotation required to maintain a film ofliquid in the desired uniform condition. Tetrachloroethylene liquid has a density of 1.6l at 25C and is well suited for use in such high density, low weight equipment. Flammability Tetrachloroethylene is not flammable and therefore presents no fire or explosion hazard, in the event of damage to the heated engine.
Toxicity In the event of leakage or in the case of accident when the power fluid escapes from the heat engine, low toxicity is highly desirable. Tetrachloroethylene has low toxicity: inhalation of the vapor at a concentration of ppm per 8 hour day is permissible. Tetrachloroethylene is not considered a contributory cause of smog.
The foregoing detailed description has been given for clarity of understanding only and no unnecessary limitations are to be understood therefrom. The invention is not limited to the exact details shown and described for obvious modifications will be apparent to those skilled in the art.
The embodiments of the invention in which an exclusive property of privilege is claimed are defined as follows:
l. The method of generating power in which tetrachloroethylene is vaporized at a temperature greater than 200C, the vapor is expanded and does work and is thereafter condensed and recycled, wherein liquid tetrachloroethylene is contacted with ferritic iron in an amount sufficient to provide at least 10 sq. cm. of iron per cc of tetrachloroethylene while at temperatures greater than 200C.
US00269380A 1970-09-01 1972-07-06 Generation of power using a rankine-cycle engine with tetrachloroethylene as the working fluid Expired - Lifetime US3802186A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4178754A (en) * 1976-07-19 1979-12-18 The Hydragon Corporation Throttleable turbine engine
US4204401A (en) * 1976-07-19 1980-05-27 The Hydragon Corporation Turbine engine with exhaust gas recirculation
US20130133328A1 (en) * 2010-08-26 2013-05-30 Michael Joseph Timlin, III The Timlin Cycle - A Binary Condensing Thermal Power Cycle
WO2017207615A1 (en) * 2016-06-01 2017-12-07 Againity Ab An expander, an organic rankine cycle system comprising such an expander and a method of producing an organic rankine cycle system comprising such an expander

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR526733A (en) * 1919-02-03 1921-10-13 William Thomas Robinson Bindle Motive Power Generators Improvements
US2371644A (en) * 1942-10-01 1945-03-20 Westvaco Chlorine Products Cor Degreasing process
US3237403A (en) * 1963-03-19 1966-03-01 Douglas Aircraft Co Inc Supercritical cycle heat engine
US3512357A (en) * 1968-05-07 1970-05-19 Douglas R Paxton Power fluid
US3527703A (en) * 1967-12-28 1970-09-08 Dow Chemical Co Polychloroethylene stabilized by metallic benzoates

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR526733A (en) * 1919-02-03 1921-10-13 William Thomas Robinson Bindle Motive Power Generators Improvements
US2371644A (en) * 1942-10-01 1945-03-20 Westvaco Chlorine Products Cor Degreasing process
US3237403A (en) * 1963-03-19 1966-03-01 Douglas Aircraft Co Inc Supercritical cycle heat engine
US3527703A (en) * 1967-12-28 1970-09-08 Dow Chemical Co Polychloroethylene stabilized by metallic benzoates
US3512357A (en) * 1968-05-07 1970-05-19 Douglas R Paxton Power fluid

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
The Condensed Chemical Dictionary, 6th Edition, by Arthur Rose et al., Reinhold Publishing Corp.; N.Y. (Definition of Perchloroethylene, Page No. (Unknown) Fifth Edition dated 1965. *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4178754A (en) * 1976-07-19 1979-12-18 The Hydragon Corporation Throttleable turbine engine
US4204401A (en) * 1976-07-19 1980-05-27 The Hydragon Corporation Turbine engine with exhaust gas recirculation
US20130133328A1 (en) * 2010-08-26 2013-05-30 Michael Joseph Timlin, III The Timlin Cycle - A Binary Condensing Thermal Power Cycle
US11028735B2 (en) * 2010-08-26 2021-06-08 Michael Joseph Timlin, III Thermal power cycle
WO2017207615A1 (en) * 2016-06-01 2017-12-07 Againity Ab An expander, an organic rankine cycle system comprising such an expander and a method of producing an organic rankine cycle system comprising such an expander
EP3901417A1 (en) * 2016-06-01 2021-10-27 Againity AB An expander, an organic rankine cycle system comprising such an expander and a method of producing an organic rankine cycle system comprising such an expander

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