GB732448A - Improvements in or relating to method and apparatus for deriming a heat interchangeand for fractionating air - Google Patents

Improvements in or relating to method and apparatus for deriming a heat interchangeand for fractionating air

Info

Publication number
GB732448A
GB732448A GB14666/52A GB1466652A GB732448A GB 732448 A GB732448 A GB 732448A GB 14666/52 A GB14666/52 A GB 14666/52A GB 1466652 A GB1466652 A GB 1466652A GB 732448 A GB732448 A GB 732448A
Authority
GB
United Kingdom
Prior art keywords
cold
passage
low pressure
interchanger
air
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
Application number
GB14666/52A
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.)
Air Products Inc
Original Assignee
Air Products Inc
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
Application filed by Air Products Inc filed Critical Air Products Inc
Publication of GB732448A publication Critical patent/GB732448A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Abstract

732,448. Cold separation of gases. AIR PRODUCTS, Inc. June 11, 1952 [June 12, 1951], No. 14666/52. Addition to 666,914. Class 8 (2). In a method of deriming a heat interchanger 221 having a common passage 227 in which there is alternate flow in opposite directions of compressed gas, e.g. air, to be rectified in a two-stage column 270 and a cold low pressure returning component e.g. nitrogen, from the low pressure column 272 and comprising passing through a passage 257 of the interchanger high pressure component gas in the direction opposite to that of the compressed gas and in heat exchange therewith and then expanding the warmed high pressure component gas, e.g. in a turbine 261, and adding it at a point 265 to the same low pressure component gas flowing to the common passage, the supplemental passage 257 is confined to adjacent the cold end of the common passage 227. As shown, the interchanger 221 has common passages 227, 237 traversed by air and low pressure nitrogen and a passage 247 traversed by product oxygen. A second interchanger 222 has similar passages 228, 238, 248 and a supplemental passage 258, one or other of the common passages of each interchange being traversed by air or returning nitrogen according to the setting of switching valves 220, 231, 229. In a modification incoming air is divided prior to compression and preliminary separation of carbon-dioxide into a 33 : 67 ratio and the portions traverse heat interchangers in parallel ; the minor portion only being cooled by cold high pressure nitrogen traversing a supplemental path at the cold end of the interchanger traversed by said minor portion, the mass of which is greater than that of the cold low pressure nitrogen flowing in the opposite direction. In a further modification wherein the incoming air is divided at a point 301, Fig. 4, into a 33 : 67 ratio and wherein said minor portion only is cooled by cold returning high pressure nitrogen traversing a path 346 at the cold end of the interchanger 333, about 5 per cent of the cold returning low pressure nitrogen traversing the exchanger 309 and serving to cool said major portion of incoming air is bled off through a valved duct 376 and a passage 374 at the warm end of the exchanger 333. The cold low pressure nitrogen enters the interchangers 309, 333 in the proportions 72 and 28 per cent. respectively.
GB14666/52A 1951-06-12 1952-06-11 Improvements in or relating to method and apparatus for deriming a heat interchangeand for fractionating air Expired GB732448A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US732448XA 1951-06-12 1951-06-12

Publications (1)

Publication Number Publication Date
GB732448A true GB732448A (en) 1955-06-22

Family

ID=22112603

Family Applications (1)

Application Number Title Priority Date Filing Date
GB14666/52A Expired GB732448A (en) 1951-06-12 1952-06-11 Improvements in or relating to method and apparatus for deriming a heat interchangeand for fractionating air

Country Status (1)

Country Link
GB (1) GB732448A (en)

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