GB700852A - Improvements in and relating to evaporating plant - Google Patents

Improvements in and relating to evaporating plant

Info

Publication number
GB700852A
GB700852A GB686850A GB686850A GB700852A GB 700852 A GB700852 A GB 700852A GB 686850 A GB686850 A GB 686850A GB 686850 A GB686850 A GB 686850A GB 700852 A GB700852 A GB 700852A
Authority
GB
United Kingdom
Prior art keywords
calandria
separator
liquor
compartment
outlet
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
GB686850A
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.)
WILLIAM WOOD HUTCHESON
Original Assignee
WILLIAM WOOD HUTCHESON
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 WILLIAM WOOD HUTCHESON filed Critical WILLIAM WOOD HUTCHESON
Priority to GB686850A priority Critical patent/GB700852A/en
Publication of GB700852A publication Critical patent/GB700852A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/06Evaporators with vertical tubes
    • B01D1/12Evaporators with vertical tubes and forced circulation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

In an evaporator comprising a plurality of calandria sections in association with a liquid/vapour separator, the liquid-outlet of each calandria section, except the last, is connected directly, or indirectly, through the separator, to the liquid-inlet of the next calandria section so that the liquid flows through the calandria sections in sequence without circulation, except if desired through the last section; and the vapour-outlet of each calandria section leads the vapours evolved in <PICT:0700852/III/1> <PICT:0700852/III/2> <PICT:0700852/III/3> that section, without passage through the tubes of the following sections, to the separator. The calandria sections may be separate, or they may be incorporated in a single housing. The apparatus may be used for concentrating milk and malt extract. In Figs. 1 and 2, the apparatus comprises four steam-heated calandria A, B, C, D, and a separator 1, which may be evacuated through outlet 3. Fresh liquor is introduced through pipe 14 into the lower end-chamber of calandria A, and the liquor is maintained at a level of about two-thirds the height of the calandria. A film of liquor rises in the tubes of the calandria, and a mixture of liquor and vapour flows into separator 1. The base of the separator is divided by two partitions 4 into four compartments, which are open at the top, and have bottom-outlets a, b, c, d. The calandria and separator compartments are connected together by piping so that the upper end-chamber of calandria A leads into the first compartment, outlet a is connected to the lower end-chamber of calandria B, the upper end-chamber of calandria B leads into the second compartment, outlet b is connected to the lower end-chamber of calandria C, and so on. Vapour is drawn off from the liquor each time it passes through the separator. The concentrated liquor is discharged from the last compartment through outlet d and pipe 15. Suspended solids in the vapours rising through the upper portion of the separator are removed by a "save-all" device, which comprises conical ledge 16 and cap 18. The solids collected in the channel formed by ledge 16 are returned through an aperture (not shown) to the first compartment. The partition walls 4 may be curved instead of straight, in order to encourage turbulence in the liquor discharged into the compartments. The calandria may be inclined, instead of being vertical. In Fig 6, three calandria sections are built into a common housing 19, the bottom and upper chambers of which are separated into compartments by partitions 20, 21 respectively. Each compartment of the upper chamber communicates by an outlet 30 with a manifold 31 which leads by condut 24 to separator 1. The fresh liquor is introduced through inlet 22, flows up the tubes of the first calandria section, and then down conduit 23 to the bottom compartment of the second calandria section; it then passes through the second and third calandria sections. Vapour is withdrawn into the separator each time the liquor emerges into an upper calandria compartment. The concentrated liquor is withdrawn through pipe 26.
GB686850A 1950-03-20 1950-03-20 Improvements in and relating to evaporating plant Expired GB700852A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB686850A GB700852A (en) 1950-03-20 1950-03-20 Improvements in and relating to evaporating plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB686850A GB700852A (en) 1950-03-20 1950-03-20 Improvements in and relating to evaporating plant

Publications (1)

Publication Number Publication Date
GB700852A true GB700852A (en) 1953-12-09

Family

ID=9822238

Family Applications (1)

Application Number Title Priority Date Filing Date
GB686850A Expired GB700852A (en) 1950-03-20 1950-03-20 Improvements in and relating to evaporating plant

Country Status (1)

Country Link
GB (1) GB700852A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0200990A2 (en) * 1985-04-30 1986-11-12 Uop Vertical tube reactor with serial downward flow through a plurality of sets of particulate containing tubes

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0200990A2 (en) * 1985-04-30 1986-11-12 Uop Vertical tube reactor with serial downward flow through a plurality of sets of particulate containing tubes
EP0200990A3 (en) * 1985-04-30 1987-05-20 Uop Inc. Vertical tube reactor with serial downward flow through a plurality of sets of particulate containing tubes

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