Abstract: A system for deaerating a liquid comprises a separation vessel where deaerated liquid is separated from gas, predominantly air; a liquid inlet to the separation vessel through which the liquid enters the separation vessel; a liquid outlet from the separation vessel through which a deaerated liquid exits the separation vessel, and a gas outlet through which the gas exits the separation vessel. The liquid inlet is arranged at a first end of the separation vessel and is configured to give the liquid entering the separation vessel a trajectory, and wherein a stop plate is arranged in the trajectory to abruptly stop the propagation of liquid travelling along the trajectory.

Abstract: The method comprises providing a first flow of liquid through a predetermined geometry, determining the flow rate through the geometry and the pressure drop across the geometry for the first flow of liquid; providing a second flow of liquid through a predetermined geometry, determining the flow rate through the geometry and the pressure drop across the geometry for the second flow of liquid, and calculating the consistency and the flow behaviour index for the liquid using the geometries and the flow rate and pressure drop for the first and second flow of liquid.

Abstract: In a method for deaerating a liquid the liquid is pressurized to a pressure above atmospheric, after which it is guided to an upstream end of a nucleation valve. A low pressure resides on the downstream end of the nucleation valve and as the liquid passes the valve, bubble nucleation is initiated, forming the first step in a deaeration process. According to the method the temperature and pressure on the downstream side of the valve is controlled such that the static pressure is above the saturation pressure, while the lowest pressure as the liquid passes the valve is below or equal to the saturation pressure.

Abstract: A pulsation damper configured to reduce pressure variations in a pipe system. The pulsation damper comprises a first pipe section and a second pipe section. The first pipe section is at least partly placed inside the second pipe section such that a product flow can flow through the first pipe section and then through a space formed between the first pipe section and the second pipe section. Due to the increased cross sectional area of the second pipe section pressure variations can be damped efficiently.

Abstract: A pulsation damper configured to reduce pressure peaks in a pipe system. The pulsation damper comprises an elastic pipe section arranged to be in a small volume state or a large volume state. A first volume held in the elastic pipe section in the large volume state is greater than a second volume held in the elastic pipe section in the small volume state. The elastic pipe section has an elliptical cross section in the small volume state. A ratio between a major axis and a minor axis of the elastic pipe section is in the range 1.05 to 10.0, such as 1.1 to 1.5.

Abstract: In a method for deaerating a liquid the liquid is pressurized to a pressure above atmospheric, after which it is guided to an upstream end of a nucleation valve. A low pressure resides on the downstream end of the nucleation valve and as the liquid passes the valve, bubble nucleation is initiated, forming the first step in a deaeration process.

Abstract: It is provided an apparatus for detecting a transition from a first phase to a second phase in a processing line. The apparatus comprises a first sensor for gathering data indicating product concentration, a second sensor for gathering data indicating product concentration. The first sensor is placed upstream of the second sensor. Further, the apparatus comprises a control device configured to receive a first data set from the first sensor and a second data set from the second sensor, and to calibrate the second sensor by comparing the second data set with the first data set.

Abstract: The disclosure relates to a method of monitoring the stay time in a restricted conduit, such as a holding tube in a heat treatment plant. A first measurement registration x of a chemical or physical magnitude, such as the temperature, takes place in the beginning of the restricted conduit. A second measurement registration y of the same chemical or physical magnitude, i.e. the temperature, takes place in the end of the restricted conduit. X and y measure natural temperature variations in the product for which the intention is to control the stay time. The stay time is determined by the time lag t at the best co-variation between x and y. By filtering the measurement registration for y, it is possible to refine the measurement method and compensate for dispersion in the product.

Abstract: The disclosure relates to a method of monitoring the stay time in a restricted conduit, such as a holding tube in a heat treatment plant. A first measurement registration x of a chemical or physical magnitude, such as the temperature, takes place in the beginning of the restricted conduit. A second measurement registration y of the same chemical or physical magnitude, i.e. the temperature, takes place in the end of the restricted conduit.X and y measure natural temperature variations in the product for which the intention is to control the stay time. The stay time is determined by the time lag t at the best co-variation between x and y. By filtering the measurement registration for y, it is possible to refine the measurement method and compensate for dispersion in the product.

Abstract: The invention relates to a method for continuously deaerating a liquid. The method comprises the step that the liquid is led into a closed container (1) so that a liquid surface (7) is formed within the container (1). The space above the liquid surface (7) is under vacuum. The method further includes the step that a gas is led into the liquid at a level below the liquid surface (7). The invention also relates to an apparatus which comprises a closed container (1). The container (1) has an inlet (5) for the liquid which is to be deaerated, as well as an outlet (6) for the liquid which has been deaerated, both placed in the lower region of the container (1). The container (1) further has a connection (13) to a vacuum pump (14) placed in the upper region of the container (1), as well as an inlet (15) for a gas placed in the lower region of the container (1).

Abstract: The invention relates to a method for continuously deaerating a liquid. The method comprises the step that the liquid is led into a closed container (1) so that a liquid surface (7) is formed within the container (1). The space above the liquid surface (7) is under vacuum. The method further includes the step that a gas is led into the liquid at a level below the liquid surface (7). The invention also relates to an apparatus which comprises a closed container (1). The container (1) has an inlet (5) for the liquid which is to be deaerated, as well as an outlet (6) for the liquid which has been deaerated, both placed in the lower region of the container (1). The container (1) further has a connection (13) to a vacuum pump (14) placed in the upper region of the container (1), as well as an inlet (15) for a gas placed in the lower region of the container (1).

Abstract: The disclosure relates to a method of regulating the level in a buffer tank (4). By means of conduits (2, 6), the tank (4) is connected to different parts in or peripheral to a process (1). There is an inflow F1 in the incoming conduit (2) and an outflow F2 in the outgoing conduit (6). The method comprises periodic measurements of the inflow F1 and also of the level L of the product which is held in the tank (4). The method also encompasses calculated and indicated level norm values which are indicated such that the level norm value is high when the outflow F2 out of the tank (4) is slight and the level norm value is low when the outflow F2 out of the tank (4) is great.