| 摘要 |
<p>1,063,560. Heat-treating liquids. SULZER BROTHERS Ltd. Dec. 23, 1965 [Jan. 15, 1965], No. 54673/65. Heading A2D. [Also in Division B8] A heat treatment plant for liquids, such as milk, has means for heating the liquid under pressure by bringing it into contact with steam and then cooling the liquid by pressure reduction, a flow setting device adjustable to a fixed value in the path of the liquid to the steam heating means, a volumetric delivery device downstream of the expansion means, and a sensing element between the expansion means and the volumetric delivery device, the sensing element being arranged to respond to the amount of liquid flowing past it and to deliver a signal to regulate the amount of liquid leaving the delivery device. The liquid for treatment is fed from a storage tank 11 through a float valve 15 to an intermediate tank 13 from which it is pumped by a metering pump 17 through a heat exchanger 23 to a heating system 21 in which live steam is injected into the liquid and thence via a pressure maintaining valve 25<SP>1</SP> into an expansion chamber 25. The pump 17 is driven by a motor 18 which is set to run at one of three speeds according to how many of three package filling machines 50, 51, 52 is in use, the speeds being set so that the pump 17 supplies a quantity of liquid through the plant and thence to a delivery pipe 37 which quantity is about 5% in excess of that required to feed the number of filling machines 50, 51, 52 in use. Liquid accumulating in the bottom of the chamber 25 flows continuously to a centrifugal pump 28 through a chamber 30 of a diaphragm sensing element 31 to a homogenizing metering pump 36 and thence to the filling machines 50, 51, 52. A second chamber 33, separated by a diaphragm 32 from the chamber 30 of the element 31, is supplied with an adjustable pressure through a pipe 34. A change in liquid flow rate through the chamber 30 produces a change in pressure which acts on the diaphragm 32. This activates a rod 38 which adjusts a belt 42 running over conical rollers 40, 41 and thence adjust the speed of the drive from a motor 43 applied to the pump 36. Excess liquid supplied to the pipe 37 is returned via a pressure maintaining valve 54 to the intermediate tank 13. In another embodiment, Fig. 2 (not shown), the pump 36 is run at a rate in excess of the maximum required and a diaphragm sensing element actuates a valve allowing excess liquid to return from the output side of the pump 36 to the sensing element chamber. In a further embodiment, Fig. 3 (not shown), a float level control is used to adjust the belt drive 42 to the pump 36. In yet another embodiment, Fig. 4 (not shown), the two metering pumps are driven by a common variable speed motor, the homogenizing pump having the Fig. 2 embodiment control means.</p> |
