Process and installation for applying a controllable heat-exchange in regenerative heat-exchanger

• US 4,610,298 A
• Filed: 07/09/1985
• Issued: 09/09/1986
• Est. Priority Date: 12/08/1981
• Status: Expired due to Term

• Current Assignee: Stork Amsterdam BV
• Original Assignee: Stork Amsterdam BV
• Inventors: van Schagen, Hans W., Goede, Rodolphe H., Tewes, Johannes W.
• Primary Examiner(s): NOT, DEFINED
• Assistant Examiner(s): Smith, Randolph A.
• Application Number:
  US06/753,261
• Time in Patent Office: 427 Days
• Field of Search: 165/39, 165/66, 165/140, 165/141, 165/142, 165/155, 165/166, 165/167, 165/909
• US Class Current: 165/299
• CPC Class Codes: A23C 3/033 and progressively transported through the apparatus
• CPC Class Codes: A23C 3/0332 in contact with multiple heating plates
• CPC Class Codes: A23L 3/18 while they are progressively transported through the apparatus
• CPC Class Codes: F28F 27/00 Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus control arrangements in general G05
• CPC Class Codes: Y10S 165/909 Regeneration

Abstract

A process and an installation for the heat treatment of a product liquid based on the continuous flow principle, in which a regenerative heat-exchanger is used in conjunction with a high temperature heater for product liquid. A part of the heat-exchanger is provided with an additional heat-exchanging surface which is connected to a cooling circuit, the variable capacity of which is determined and controlled by both the temperature and the output of the product liquid, whereby to maintain the efficiency of the heat treatment under changing input quantities of the product liquid. Control, above is effected by a combination temperature sensor interconnected to the product liquid conduit directed to the high temperature heater and a flow rate sensor interconnected to another given portion of the product liquid conduit.

Claims

1. In a heat-treatment plant for heat treatment of a product liquid of continuous flow, a high temperature heater and a regenerative heat-exchanger connected thereto, the regenerative heat exchanger having counterflow heat exchange between product liquid entering and leaving the high temperature heater, said regenerative heat exchanger including a cooling liquid passage with a heat exchanging surface for withdrawing heat from the product liquid going to the high temperature heater, a cooling liquid conduit interconnected to the cooling liquid passage, said cooling liquid conduit including a flow control which is reactive to temperature and flow rate of the product liquid, the control having a temperature sensor interconnected to the product liquid conduit leading to the high temperature heater and a flow rate sensor interconnected to the product liquid conduit.

2. A regenerative heat exchanger according to claim 1 wherein the heat exchanger is of concentric tubular construction comprising a set of three concentric tubes which together form three channels, whereby preheated product liquid going to the high temperature heater is conducted through one intermediate channel and cooling liquid through one preselected innermost and outermost channel and wherein heated product liquid leaving the high temperature heater is selectively conducted through the opposite of said outermost and innermost channels.

3. A regenerative heat exchanger according to claim 1 wherein the heat exchanger is of plural plate construction, the respective plates defining pre-heated and heated liquid passage apertures and an extra set of cooling liquid passage apertures intermediately disposed with respect to the first said apertures for the passage of cooling liquid.