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US1396024A - Refrigeration process - Google Patents

Refrigeration process Download PDF

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Publication number
US1396024A
US1396024A US236370A US23637018A US1396024A US 1396024 A US1396024 A US 1396024A US 236370 A US236370 A US 236370A US 23637018 A US23637018 A US 23637018A US 1396024 A US1396024 A US 1396024A
Authority
US
United States
Prior art keywords
propylene
refrigeration process
refrigerant
refrigerants
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US236370A
Inventor
Albert G Crawford
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HALLECK W SEAMAN
Original Assignee
HALLECK W SEAMAN
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=22889202&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=US1396024(A) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by HALLECK W SEAMAN filed Critical HALLECK W SEAMAN
Priority to US236873A priority Critical patent/US1439728A/en
Priority to US236370A priority patent/US1396024A/en
Priority to AT90995D priority patent/AT90995B/en
Priority to AT90994D priority patent/AT90994B/en
Priority to FR518863A priority patent/FR518863A/en
Priority to FR518862A priority patent/FR518862A/en
Priority to GB20690/20A priority patent/GB148874A/en
Publication of US1396024A publication Critical patent/US1396024A/en
Application granted granted Critical
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/02Materials undergoing a change of physical state when used
    • C09K5/04Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
    • C09K5/041Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
    • C09K5/042Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising compounds containing carbon and hydrogen only

Definitions

  • My invention has reference more particucommercial use in ice making, in cold stor age plants or for general refrigeration puroses.
  • refrigerants now commonly used such as ammonia gas, sulfur dioxid gas, and ethylchlorid, are objectionable for the reason that they are not only poisonous and corrosive to the pipes and receptacles in which they are used, but most of them as well as carbon dioxid, also require a high pressure and consequently a heavy installation in order to condense themvinto the liquid state.
  • the propylene is introduced into a circulating system consisting of a compresser which applies pressureto the gas and re Jerusalem it to a liquid form, and the liquid, after being suitably cooled to dissipate the heat of compression, is led to and allowed tov evaporate in proximity to the material or compartment which is to be cooled, and as the evaporation takes place heat is absorbed thereby and a reduction in temperature takes place around the point at which the evaporation takes place.
  • the gas resulting from the evaporation is then lead back to the compresser and again liquefied by pressure and a continuous circulation thereof is thereby maintained, the propylene being alternately compressed and liquefied and then expanded so as to continuously absorb heat and maintain the desired low temperature.
  • a refrigerating process which comprises compressing substantially pure propylene gase to liquefy the same, and evaporating the liquid by relieving the pressure thereon to extract heat from adjacent material.
  • a refrigeration process which comprises compressing a non-acid gas having a hydrocarbon content consisting chiefly of propylene to liquefy the propylene, and evaporating the liquid by relieving the pres sure thereon to extract heat from adjacent materials.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Thermal Sciences (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)

Description

.larly to a refrigerant and the process of using the same whereby 1t is adapted for urrso STATES T iii ALBERT Gr. CRAWFORD, OF CHICAGO, ILLINOIS, ASSIGNOR T0 HALLEGK 'W. SEAMAN, 01? CLINTON, IOWA.
nnrnrenna'rron rnocrss.
Ito Drawing.
To all whom it may concern Be it known that T, ALBERT G. CRAWFORD, a citizen of the United States, and a resi dent of the city of Chicago, in the county of Cook and State of Illinois, have invented certain new and useful Improvements in a Refrigeration Process; and I do hereby declare that the following is a full, clear, and exact description of the same.
My invention has reference more particucommercial use in ice making, in cold stor age plants or for general refrigeration puroses. p The refrigerants now commonly used, such as ammonia gas, sulfur dioxid gas, and ethylchlorid, are objectionable for the reason that they are not only poisonous and corrosive to the pipes and receptacles in which they are used, but most of them as well as carbon dioxid, also require a high pressure and consequently a heavy installation in order to condense themvinto the liquid state.
It is an object of this invention, therefore, to provide a medium which may be utilized for carrying on the] process of refrigeration or ice making and which not only requires a lower pressure and consequently a lighter and less-expensive installation to utilize the same, but'which is also unaccompanied with the danger of poisoning and does not have the corrosive action on. the apparatus as the refrigerants heretofore used.
I have found that propylene of the formula C ll having a boiling point of -5 0 G, gives excellent results as a refrigerant. It is easily liquefiable under cold or pressure and does not decompose after being used for a long time in a refrigerating machine, and my experiments show that very low temperatures can be .obtained by using this material as a refrigerant.
The refrigerating process using propylene as the refrigerant is carried vout by using this refrigerant in a manner similar to that in which refrigerants have been used hereto- Specification of Letters Patent.
Application filed. May 27, 1918. Serial No. 236,870.
fore, except that it requires less pressure to condense and liquify than with some of the refrigerants heretofore employed, a lighter installation may be used and it is unnecessary to provide-precautions against cor-' rosion and poisonous gas as with refrigerants heretofore employed.
The propylene is introduced into a circulating system consisting of a compresser which applies pressureto the gas and re duces it to a liquid form, and the liquid, after being suitably cooled to dissipate the heat of compression, is led to and allowed tov evaporate in proximity to the material or compartment which is to be cooled, and as the evaporation takes place heat is absorbed thereby and a reduction in temperature takes place around the point at which the evaporation takes place. The gas resulting from the evaporation is then lead back to the compresser and again liquefied by pressure and a continuous circulation thereof is thereby maintained, the propylene being alternately compressed and liquefied and then expanded so as to continuously absorb heat and maintain the desired low temperature.
v I claim as my invention:
1. A refrigerating process which comprises compressing substantially pure propylene gase to liquefy the same, and evaporating the liquid by relieving the pressure thereon to extract heat from adjacent material. I
2. A refrigeration process which comprises compressing a non-acid gas having a hydrocarbon content consisting chiefly of propylene to liquefy the propylene, and evaporating the liquid by relieving the pres sure thereon to extract heat from adjacent materials.
In testimony whereof I have hereunto subscribed my name in the presence of two subscribing witnesses.
ALBERT G. CRAWFORD. Witnesses:
' LAWRENCE REIBSTEIN,
FRANK A. BREMER, Jr.
US236370A 1918-05-27 1918-05-27 Refrigeration process Expired - Lifetime US1396024A (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
US236873A US1439728A (en) 1918-05-27 1918-05-27 Refrigerating process
US236370A US1396024A (en) 1918-05-27 1918-05-27 Refrigeration process
AT90995D AT90995B (en) 1918-05-27 1920-07-01 Equipment for compression refrigeration machines.
AT90994D AT90994B (en) 1918-05-27 1920-07-01 Equipment for compression refrigeration machines.
FR518863A FR518863A (en) 1918-05-27 1920-07-05 Refrigerant and refrigeration process
FR518862A FR518862A (en) 1918-05-27 1920-07-05 Refrigerant product and refrigeration process
GB20690/20A GB148874A (en) 1918-05-27 1920-07-10 Refrigerant and process of refrigeration

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US236873A US1439728A (en) 1918-05-27 1918-05-27 Refrigerating process
US236370A US1396024A (en) 1918-05-27 1918-05-27 Refrigeration process

Publications (1)

Publication Number Publication Date
US1396024A true US1396024A (en) 1921-11-08

Family

ID=22889202

Family Applications (2)

Application Number Title Priority Date Filing Date
US236873A Expired - Lifetime US1439728A (en) 1918-05-27 1918-05-27 Refrigerating process
US236370A Expired - Lifetime US1396024A (en) 1918-05-27 1918-05-27 Refrigeration process

Family Applications Before (1)

Application Number Title Priority Date Filing Date
US236873A Expired - Lifetime US1439728A (en) 1918-05-27 1918-05-27 Refrigerating process

Country Status (4)

Country Link
US (2) US1439728A (en)
AT (2) AT90995B (en)
FR (2) FR518862A (en)
GB (1) GB148874A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3249546A (en) * 1963-10-30 1966-05-03 Du Pont Azeotrope refrigerant compositions
AU3504584A (en) * 1983-10-25 1985-05-22 Marzouki, M. Etc. Enceinte frigorigene procede de refroidissement sans source froide externe

Also Published As

Publication number Publication date
GB148874A (en) 1921-10-10
US1439728A (en) 1922-12-26
AT90995B (en) 1923-01-25
FR518863A (en) 1921-06-01
AT90994B (en) 1923-01-25
FR518862A (en) 1921-06-01

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