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    • 4. 发明公开
    • METHOD COMPRISING SEPARATION AND HIGH VOLTAGE PULSE TREATMENT BEFORE DIGESTION OR FURTHER PURIFICATION
    • VERFAHREN MIT TRENNUNG UND HOCHSPANNUNGSPULSBEHANDLUNG VOR DER VERDAUUNG ODER WEITEREN REINIGUNG
    • EP3066055A4
    • 2017-08-02
    • EP14859855
    • 2014-11-04
    • ARC AROMA PURE AB
    • HENRIKSSON PÄR H
    • C02F1/48B63J4/00C02F1/00C02F1/46C02F11/02C02F11/04C02F11/12C02F11/14C02F11/18C12P5/02
    • C02F1/4608A23L5/30A23V2002/00B01D35/06B63J4/00B63J4/002C02F1/001C02F1/30C02F1/32C02F1/36C02F1/52C02F11/006C02F11/02C02F11/10C02F11/121C02F11/14C02F11/185C02F2103/008C02F2201/46175C02F2303/04Y02T70/36Y02W10/27
    • The present invention describes a method of treatment of at least one phase, solid and/or liquid, of a pumpable liquid flow, wherein the method comprises first filtration for separation of a liquid phase from the pumpable liquid flow, for obtaining one flow with increased content of solid phase and one flow with increased liquid level; and thereafter treatment of the flow with increased content of solid phase with high voltage pulses in a PEF-unit. Furthermore, the present invention is also related to a system for treatment of at least one phase, solid and/or liquid, of a pumpable liquid flow and the use of such a system, such as use for the treatment of at least one phase, solid and/or liquid, of a pumpable liquid foodstuff or a ballast water flow, or as a pre-treatment before digestion. Furthermore, the present invention also refers to a method of treatment of at least one phase, solid and/or liquid, of a pumpable liquid flow, wherein the method comprises hygienization of at least a part of the pumpable liquid flow in an IR-chamber; and treatment of at least a part of the pumpable liquid flow with high voltage pulses in a PEF-unit, wherein the hygienization in the IR-chamber may be performed before or after, or both before and after, the treatment with high voltage pulses in a PEF-unit.
    • 本发明描述了一种处理至少一个可泵送液体流的固体和/或液体相的方法,其中该方法包括第一次过滤以从可泵送液体流中分离液相,以获得具有增加的流量 固相含量和液位升高时的流量; 然后在PEF单元中用高电压脉冲处理具有增加的固相含量的流。 此外,本发明还涉及一种用于处理至少一个可泵送液体流的固体和/或液体相的系统以及这种系统的用途,例如用于处理至少一个相, 固体和/或液体,可泵送液体食品或压载水流,或作为消化前的预处理。 此外,本发明还涉及一种处理至少一个可泵送液体流的固体和/或液体相的方法,其中该方法包括将可泵送液体流的至少一部分卫生化到IR室 ; 以及在PEF单元中用高电压脉冲处理至少一部分可泵送液体流,其中可在用高压脉冲处理之前或之后或之前和之后执行IR室中的卫生化 一个PEF单元。
    • 9. 发明公开
    • PROCÉDÉ DE CARBONISATION HYDROTHERMALE OPTIMISÉ ET INSTALLATION POUR SA MISE EN OEUVRE
    • 最佳HYDROTHERMALES KARBONISIERUNGSVERFAHREN UND ANLAGE ZUR IMPLEMENTIERUNG DAVON
    • EP3022158A1
    • 2016-05-25
    • EP14767107.7
    • 2014-07-15
    • Degrémont
    • PARDO, Pierre EmmanuelBOURDAIS, Jean Louis
    • C02F11/10F23G5/027F23G7/00C02F11/12C02F1/66F23G5/00
    • C02F11/10C02F1/66C02F11/12C02F2209/02C02F2209/03C02F2301/066C02F2303/22F23G5/0273F23G7/001Y02W10/40
    • A method and corresponding facility for the hydrothermal carbonisation of pasty products or waste, or sewage treatment plant sludge, in a pressurised reactor (3) heated to carbonisation temperature T0, generally between 140 °C and 280 °C. According to the method, before being inserted into the reactor, the products to be treated undergo the following steps: pressurisation, preheating in an exchanger (2), by a thermal fluid that flows in a closed loop, and that receives heat from the products coming out of the reactor; the thermal fluid is heated in the loop by an external heat source (12), downstream from the exchange with the products coming out of the reactor, and upstream from the preheating of the products entering the reactor, and the temperature of the product to be treated, preheated by the thermal fluid, when it enters the reactor (3), is between the carbonisation temperature T0 and T0 - 100°C. Moreover, the product to be treated flows in at least one tube (1b), including in the preheating exchanger (2), until it enters the reactor (3), and in at least one location of the tube (1b), liquid is injected (20) to create a liquid ring (A) against the inner wall of the tube (1b), and reduce the pressure drops.
    • 在加热到碳化温度T0的加压反应器中,将糊状产物或废物或污水污泥进行水热碳化的方法和设备。 在进入反应器之前,产品经过交换器中的加压和预热,通过在闭合回路中流动的热流体和从离开反应器的产物接收热量; 热流体在环路中被外部热源加热,与离开反应器的产物的交换下游,以及进入反应器的产品的预热上游,以及待处理的产品的温度,由 热流体在进入反应器时处于碳化温度T0和T0-100℃之间。待处理的产品在至少一个管中流动,其中至少一个位置中注入液体以产生液环 抵靠内壁,并减少压降。