US654395A - Absorption refrigerating apparatus. - Google Patents

Absorption refrigerating apparatus. Download PDF

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US654395A
US654395A US68993898A US1898689938A US654395A US 654395 A US654395 A US 654395A US 68993898 A US68993898 A US 68993898A US 1898689938 A US1898689938 A US 1898689938A US 654395 A US654395 A US 654395A
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exhaust
pipe
pumps
chamber
steam
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US68993898A
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Nicolai H Hiller
Henry Torrance Jr
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0012Recuperative heat exchangers the heat being recuperated from waste water or from condensates

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  • Our invention relates to Various new and useful improvements in refrigerating apparatus of the absorption type; and the essential object of our invention is to economize the operation of such apparatus.
  • Figure 1 represents a diagrammatic view of one form of our invention as the same will be preferably carried out in connection with arefrigerating apparatus of the absorption type wherein three separate pumps are used, one for circulating the ammonia, another for supplying water to the condenser, and the third for circulating the brine; and Fig. 2, asimilar View illustrating the application of our inven- In all refrigerating-1n achines of When th pa t s,
  • FIG. 4 is an ammonia-pump for circulating the ammonia through the apparatus, and 5 a water-pump for supplying the condenser with cooling-water.
  • a brinepump 6 which will be used when a cooler is employed for circulating brine to and from said cooler and through the brinepipes.
  • the several pumps are all operated from a single boiler through a live-steam pipe 7 and branch pipes 8 S 8, leading to each of said pumps.
  • An exhaust-pipe 9 leads from each pump to an exhaust-chamber 10, of suflicient capacity.
  • the exhaust-steam from the exhaust-chamber 10 is carried off by a pipe 11, which is preferably provided with an oil-separator 12 therein, by which any oil carried over with the exhauststeam will be separated and conveyed off by a drip-pipe 13, leading to adrain. Any water of condensation which may accumulate in this separator will also be carried off through said drain-pipe.
  • a blow-off pipe 14 connects with the oil-separator 12 and is provided With a safety-valve 15, set so as to automatically IOO 18 therein of any suitable type, by means of which when the pressure in the pipe 16 falls below the required point live steam mayenter through said reducing-valve from the livesteam pipe, so as to elevate the pressure to the required point.
  • the steam blown off at the safety-valve 15 may be, and preferably is, conveyed to a stack 19 through a pipe 20, and, if desired, apipe 21 may connect the exhaust-chamber 10 directly with said stack, said pipe being provided with a valve 22 therein.
  • pipe 17 is provided with a'valve 23, and the pipe 16 is provided with a valve 24 between the oil-separator and the live-steam pipe 7.
  • the safety-Valve 15 will automatically relieve the same and reduce it to the proper point. In this way it will be seen that the pressure in the coil 2 will be automatically regulated and that no live steam will be directly used unless for the purpose of automatically supplementing any deficiency in the exhauststeam. If for any purpose it is desired to heat the coil 2 by live steam alone, this may be done by closing the valve 24:, so that the live steam will pass through the reducingvalve 18 into the pipe 16, as will be understood. If, on the otherhand, for any reason it is desired to cut 0E live steam to the generator, this is effected by closing thevalve 23.. Whenever for any reason the generator is to be operated by the action of live steam alone, and in order to overcome the back pressure on the pumps, the valve 22 will be opened, so that the pumps will exhaust directly into the stack.
  • a refrigerating apparatus of the absorptiontype the combination with a generator and a series of pumps used in connection with such apparatus, of an exhaust-chamber, connections between said chamber and the exhaust-ports of said pumps, a pipe connecting said exhaust-chamber with the heatingcoil of the generator, an oil-separator in said pipe, a safety-valve also in said pipe, a stack, and a pipe connecting said exhaust-chamber with said stack, substantially as set forth.
  • a refrigerating apparatus of the absorption type the combination with a generator and a series of pumps used in connection with such apparatus, of an exhaust-chamber, connections between said chamber and the exhaust-ports of said pumps, a pipe connect ing said exhaust-chamber with the heating coil of the generator, an oil separator in said of the generator, and a reducing-valve in said 15 pipe, substantially as set forth.

Description

Patented Juli 24; I900. N. H. H ILLER & H. TORRANDE, 1n. ABSORPTION BEFBIGEBATING APPARATUS.
(Application filed Aug. 81, 1898.)
(No Model.)
Ina/anions TNE NORRIS r-zrzns co. PHOTO-HTML, wAsmNcrou, b. c.
' STATE TENT Crates.
NIOOLAI II. HILLER, OF OARBONDALE, PENNSYLVANIA, AND HENRY TORRANCE, J R. OF TENAFLY, NEW JERSEY.
ABsoRPTtoN REFRIGEIRATING APPARATUS.
srnorrrcnrron forming part of Letters Patent No. e54',ee5,uat a July 24, 19150. Ap lication filed August 31,1898. Serial No. 689,938. (N o'modelo To aZZ whom it may concern:
Be it known that we, NIOOLAI II. HILLER, of Carbondale, in the county of Lackawanna and State of Pennsylvania, and HENRY TOR- RANGE, J12, of Tena'fly, in the county of Bergen and State of New Jersey, citizens of the United States, have invented certain new and useful Improvements in Absorption Refrigerating Apparatus, of which the followingis a specification.
Our invention relates to Various new and useful improvements in refrigerating apparatus of the absorption type; and the essential object of our invention is to economize the operation of such apparatus.
In absorption refrigerating-machines as now constructed the generator is heated by live steam from a boiler, and the several pumps are also operated by steam from the same boiler. this typeana'mmonia-pump is employed for circulating the ammonia through the apparatus, and a water-pump is also used for supplying t e sqsden ris used in connection with a brine-cooler, a separate brine-circulating pump is also employed, so that in all instances at least two pumps are employed, while in many plants a third pump is used. We have found from a careful study and examination of refrigerating apparatus of this type as now constructed that the amount of steam required to operate the several pumps is frequently as great as thatused in heating the generator. By means of our invention we reduce the steamsupply necessary in theapparatus, and therefore economize in its operation.
In order that our invention may be better understood, attention is directed to the accompanying drawings, forming a part of this specification, in which Figure 1 represents a diagrammatic view of one form of our invention as the same will be preferably carried out in connection with arefrigerating apparatus of the absorption type wherein three separate pumps are used, one for circulating the ammonia, another for supplying water to the condenser, and the third for circulating the brine; and Fig. 2, asimilar View illustrating the application of our inven- In all refrigerating-1n achines of When th pa t s,
tion to a refrigerating apparatus of the type referred to wherein the three pumps are all driven froma counter-shaft operated by a single engine.
In both of the above Views corresponding parts are represented by the same numerals of reference.
1 represents the generator of an absorption refrigerating apparatus, the said generator being provided with a steam-c0112 therein, by which its contents may be heated. As the steam condenses in said coil it is carried off by a trap 3 in the usual way.
4 is an ammonia-pump for circulating the ammonia through the apparatus, and 5 a water-pump for supplying the condenser with cooling-water. We also illustrate a brinepump 6, which will be used when a cooler is employed for circulating brine to and from said cooler and through the brinepipes. When the apparatus is used with ammonia expansion-coils, as will be possible and as in some instances may be desirable, the brinepump 6 will bedispensed with; The several pumps are all operated from a single boiler through a live-steam pipe 7 and branch pipes 8 S 8, leading to each of said pumps. An exhaust-pipe 9 leads from each pump to an exhaust-chamber 10, of suflicient capacity.
to prevent the operation of the pumps from materially affecting the pressure therein. The exhaust-steam from the exhaust-chamber 10 is carried off by a pipe 11, which is preferably provided with an oil-separator 12 therein, by which any oil carried over with the exhauststeam will be separated and conveyed off by a drip-pipe 13, leading to adrain. Any water of condensation which may accumulate in this separator will also be carried off through said drain-pipe. A blow-off pipe 14 connects with the oil-separator 12 and is provided With a safety-valve 15, set so as to automatically IOO 18 therein of any suitable type, by means of which when the pressure in the pipe 16 falls below the required point live steam mayenter through said reducing-valve from the livesteam pipe, so as to elevate the pressure to the required point. The steam blown off at the safety-valve 15 may be, and preferably is, conveyed to a stack 19 through a pipe 20, and, if desired, apipe 21 may connect the exhaust-chamber 10 directly with said stack, said pipe being provided with a valve 22 therein.
To facilitate the operation of the device, pipe 17 is provided with a'valve 23, and the pipe 16 is provided with a valve 24 between the oil-separator and the live-steam pipe 7.
The operation of this device as we have described it will be as follows: Live steam from the steam-pipe 7 will operate the several pumps, and the exhaust-steam from said pumps will pass by the pipes 9 into the exhaust-chamber 10. This exhaust-steam will thence pass first to the oil-separator, by means of which any oil mechanically entrained therewith will be separated, and the exhauststeam will then pass by the pipe 16 into the coil 2, so as to heat the generator. In case the exhaust-steam thus supplied by the pumps 4, 5, and 6 is not sufficient to maintain the proper pressure in the generator-coil, live steam from the pipe 7 will automatically pass through the reducing-valve 18, so as to increase the pressure to the proper point, the said reducing-valve automatically closing when that point is reached. If, on the other hand, the exhaust-steam supplied by the pump effects a higher pressure in the coil 2 than is desired, the safety-Valve 15 will automatically relieve the same and reduce it to the proper point. In this way it will be seen that the pressure in the coil 2 will be automatically regulated and that no live steam will be directly used unless for the purpose of automatically supplementing any deficiency in the exhauststeam. If for any purpose it is desired to heat the coil 2 by live steam alone, this may be done by closing the valve 24:, so that the live steam will pass through the reducingvalve 18 into the pipe 16, as will be understood. If, on the otherhand, for any reason it is desired to cut 0E live steam to the generator, this is effected by closing thevalve 23.. Whenever for any reason the generator is to be operated by the action of live steam alone, and in order to overcome the back pressure on the pumps, the valve 22 will be opened, so that the pumps will exhaust directly into the stack.
While in the operation of the device as shown there will be a back pressure upon the pum,ps,and in consequence a larger steamsupply will be required to operate the same, yet since the exhaust-steam is utilized in whole or in part for operating the generator a very material saving will be effected.
Instead of utilizing the exhaust-steam from the several pumps, as we have explained, it will be possible to operate the several pumps from a counter-shaft 25, as shown in Fig. 2, by a single engine 26, In this case an exhaust-pipe 27 from the engine will be connected to the exhaust-chamber 10, if used, or
directly to the pipe 16, the operation of this device being the same in all other respects as that shown in Fig. 1. invention maybe desirable in some instances, because by the operation of several pumps from a counter-shaft, as explained, a material saving in the cost of operation may be effected owing to the increased efficiency of a single engine over a series of ordinary reciprocating pumps of the same capacity.
Having now described ourinvention, what we claim as new, and desire to secure by Letters Patent, is as follows: 7
1. In a refrigerating apparatus of the absorption type, the combination with a generator and a series of pumps used in connection with such apparatus, of an exhaust-chamber, connections between said chamber and the exhaust-ports of said pumps, and a pipe connecting said exhaust-chamber with the heat ing-coil of the generator, substantially as set forth.
2. In a refrigerating apparatus of the absorption type, the combination with a gener ator and a series of pumps used in connection with such apparatus, of an exhaust-chamber, connections between said chamber and the exhaust-ports of said pumps, a pipe connecting said exhaust chamber with the heating coil of the g6ll6Ptl70l,2tl1d an oil-separator in said pipe, substantially as set forth.
3. In a refrigerating apparatus of the absorption type, the combination with a gener- The latter form of our ator and a series of pumps used in connection with such apparatus, of an exhaust-chamber, connections between said chamber and the exhaust-ports of said pumps, a pipe connect ing said exhaust-chamber with the heatingcoil of the generator, an oil-separator in said pipe, and a safety-valve also in said pipe, substantially as set forth.
4. In a refrigerating apparatus of the absorptiontype, the combination with a generator and a series of pumps used in connection with such apparatus, of an exhaust-chamber, connections between said chamber and the exhaust-ports of said pumps, a pipe connecting said exhaust-chamber with the heatingcoil of the generator, an oil-separator in said pipe, a safety-valve also in said pipe, a stack, and a pipe connecting said exhaust-chamber with said stack, substantially as set forth.
5. In a refrigerating apparatus of the absorption type, the combination with a generator and a series of pumps used in connection with such apparatus, of an exhaust-chamber, connections between said chamber and the exhaust-ports of said pumps, a pipe connect ing said exhaust-chamber with the heating coil of the generator, an oil separator in said of the generator, and a reducing-valve in said 15 pipe, substantially as set forth.
This specification signed and witnessed the 18th and 27th days of August, 1898.
NIOOLAI H. HILLER. HENRY TORRANOE, JR.
Witnesses to signatureof Nicolai I-I. Hillel- A. P. HoWEs, OLIVIA H. HILLER.
Witnesses to signature of Henry Torrance, J r.
FRANK L. DYERs, S. O. EDMONDS.
US68993898A 1898-08-31 1898-08-31 Absorption refrigerating apparatus. Expired - Lifetime US654395A (en)

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