WO2020073653A1 - 冷凝式油水分离方法 - Google Patents
冷凝式油水分离方法 Download PDFInfo
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- WO2020073653A1 WO2020073653A1 PCT/CN2019/087124 CN2019087124W WO2020073653A1 WO 2020073653 A1 WO2020073653 A1 WO 2020073653A1 CN 2019087124 W CN2019087124 W CN 2019087124W WO 2020073653 A1 WO2020073653 A1 WO 2020073653A1
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- WO
- WIPO (PCT)
- Prior art keywords
- oil
- plate
- water
- separation method
- water separation
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
Definitions
- the invention relates to the technical field of oil-water separation, in particular to a condensing oil-water separation method.
- the separation methods of existing oil-water separation equipment can be roughly divided into gravity separation, centrifugal separation, electrical separation, adsorption separation, air floatation separation, etc.
- These oil-water separation methods have their own substantial defects, and the oil-water separation time is long 3.
- Low oil extraction efficiency and low oil purity For example, the gravity separation method adopts the form of a sedimentation tank, which will cause the liquid flow to exist in a dead zone, and some liquid cannot be replaced by flow. The organic matter in the water will gradually decay and smell; the air floatation separation method will A large amount of odor is generated; the maintenance of power components of centrifugal separation equipment is difficult, and currently only used in laboratory analysis equipment.
- the purpose of the present invention is to solve the shortcomings of the prior art, and to provide a condensed oil-water separation method with simple method, short oil-water separation time, high oil extraction efficiency, and high oil purity.
- a condensing oil-water separation method characterized by the difference in freezing point of oil and water, in the temperature range where oil reaches the freezing point and water does not reach the freezing point, efficient oil-liquid separation of oil and water is achieved,
- the condensing oil-water separation method of the present invention is obtained through the following steps:
- the invention also includes step 5: heating the scraped oil removal tank, so that the grease is heated to form liquid oil and quickly flow into the oil receiving barrel.
- the step 1 condensation plate of the present invention is composed of a flat plate and a cold plate evaporator, the cold plate evaporator is fixed on the flat plate, the cold plate evaporator is connected to a heat pump system, and the heat pump system is connected to a temperature control switch,
- the flat plate is made of temperature-conducting material.
- the oil removal tank in step 5 of the present invention is composed of a tank body and an oil-cooled condenser below the tank body, and the oil-cooled condenser is connected to a heat pump system.
- the temperature control switch of the present invention can adopt a PLC controller to achieve the function of automatic control.
- the invention has the advantages of novel structure, high oil extraction efficiency and high oil purity due to the adoption of the above method.
- a condensing oil-water separation method characterized by the difference in freezing point of oil and water, in the temperature range where oil reaches the freezing point and water does not reach the freezing point, efficient oil-liquid separation of oil and water is achieved,
- the condensing oil-water separation method of the present invention is obtained through the following steps:
- the invention also includes step 5: heating the scraped oil removal tank, so that the grease is heated to form liquid oil and quickly flow into the oil receiving barrel.
- the step 1 condensation plate of the present invention is composed of a flat plate and a cold plate evaporator, the cold plate evaporator is fixed on the flat plate, the cold plate evaporator is connected to a heat pump system, and the heat pump system is connected to a temperature control switch,
- the flat plate is made of temperature-conducting material.
- the oil removal tank in step 5 of the present invention is composed of a tank body and an oil-cooled condenser below the tank body, and the oil-cooled condenser is connected to a heat pump system.
- the temperature control switch of the present invention can adopt a PLC controller to achieve the function of automatic control.
- Embodiment When the present invention is in operation, the PLC controller is connected to the power supply, and the cooling and heating system cools the condensing plate and heats the deoiling condenser and the water-cooling condenser.
- the specified temperature is high
- the condenser plate descends and contacts the liquid surface.
- the oil on the liquid surface is cooled by the condenser plate to become grease and adheres to the condenser plate, and then the condenser plate is lifted and used.
- the oil scraper scrapes the grease under the condensation plate into the degreasing tank.
- the grease is heated by the oil-cooled condenser under the degreasing tank to become oil, and flows into the oil receiving barrel through the oil outlet at the bottom of the degreasing tank.
- the invention has the advantages of novel structure, high oil extraction efficiency and high oil purity due to the adoption of the above method.
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- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
一种冷凝式油水分离方法,通过油和水的凝固点不同,在油达到凝固点而水并未达到凝固点的温度范围内,实现油和水的高效油液分离,包括步骤:1)、制作冷凝板;2)、对冷凝板进行降温冷凝,使得冷凝板的温度高于水的凝固点而等于或低于油的凝固点;3)、将冷凝后的冷凝板底面放置并接触在静止后的盛有油液的机箱内的液体上表面,将悬浮在液体表面的油冷凝成油脂并粘附到冷凝板上;4)、用刮油板刮除粘附在冷凝板上的油脂。
Description
本发明涉及油水分离技术领域,具体地说是一种冷凝式油水分离方法。
众所周知,现有的油水分离设备的分离方式大致可分为重力式分离、离心式分离、电分离、吸附分离、气浮分离等,这些油水分离方式均存在各自的实质性缺陷,油水分离时间长、提油效率低、出油纯度低,如重力式分离方式采用沉降池形式,会导致液体流动存在死区,部分液体得不到流动置换,水中有机质会逐渐腐败变臭;气浮分离方式会产生大量臭气;离心式分离方式设备动力部件维护困难,目前只应用于实验室的分析设备等。
另外,上述分离方法分离出的油水由于分离不彻底,导致油品差,储存及再利用困难。
发明内容
本发明的目的在于解决现有技术的不足,提供一种方法简单、油水分离时间短、提油效率高、出油纯度高的冷凝式油水分离方法。
本发明解决其技术问题所采用的技术方案是:
一种冷凝式油水分离方法,其特征在于通过油和水的凝固点不同,在油达到凝固点而水并未达到凝固点的温度范围内,实现油和水的高效油液分离,
本发明冷凝式油水分离方法通过以下步骤得到:
1、制作冷凝板;
2、对冷凝板进行降温冷凝,使得冷凝板的温度高于水的凝固点而等于或低于油的凝固点;
3、将冷凝后的冷凝板底面放置并接触在静止后的盛有油液的机箱内的液体上表面,将悬浮在液体表面的油冷凝成油脂并粘附到冷凝板上;
4、用刮油板刮除粘附在冷凝板上的油脂;
由于油的浮力大于水和杂物而悬浮于液体表面,因此,如此反复重复上述1-4步骤,即可将油水渣分离彻底,显著提高了提油纯度和提油效率。
本发明还包括步骤5:对刮除后的除油槽进行加热,以使油脂加热后形成液体油而快速流入到接油桶中。
本发明所述步骤1冷凝板是由平板和冷板蒸发器构成,所述冷板蒸发器固定在平板上,所述冷板蒸发器与热泵系统连接,所述热泵系统与温控开关连接,所述平板是由导温材 料制成。
本发明所述步骤5除油槽是由槽体和槽体下面的油冷冷凝器构成,所述油冷冷凝器与热泵系统连接。
本发明所述温控开关可以采用PLC控制器,以达到自动控制的作用。
本发明由于采用上述方法,具有结构新颖,提油效率高,出油纯度高等优点。
下面结合附图和实施例对本发明进行说明。
一种冷凝式油水分离方法,其特征在于通过油和水的凝固点不同,在油达到凝固点而水并未达到凝固点的温度范围内,实现油和水的高效油液分离,
本发明冷凝式油水分离方法通过以下步骤得到:
1、制作冷凝板;
2、对冷凝板进行降温冷凝,使得冷凝板的温度高于水的凝固点而等于或低于油的凝固点;
3、将冷凝后的冷凝板底面放置并接触在静止后的盛有油液的机箱内的液体上表面,将悬浮在液体表面的油冷凝成油脂并粘附到冷凝板上;
4、用刮油板刮除粘附在冷凝板上的油脂;
由于油的浮力大于水和杂物而悬浮于液体表面,因此,如此反复重复上述1-4步骤,即可将油水渣分离彻底,显著提高了提油纯度和提油效率。
本发明还包括步骤5:对刮除后的除油槽进行加热,以使油脂加热后形成液体油而快速流入到接油桶中。
本发明所述步骤1冷凝板是由平板和冷板蒸发器构成,所述冷板蒸发器固定在平板上,所述冷板蒸发器与热泵系统连接,所述热泵系统与温控开关连接,所述平板是由导温材料制成。
本发明所述步骤5除油槽是由槽体和槽体下面的油冷冷凝器构成,所述油冷冷凝器与热泵系统连接。
本发明所述温控开关可以采用PLC控制器,以达到自动控制的作用。
实施例:本发明在工作时,PLC控制器接通电源,制冷制热系统对泠凝板制冷和对除油冷凝器及水冷冷凝器制热,当冷凝板达到指定温度时,该指定温度高于水的凝固点而等于或低于油的凝固点,冷凝板下行与液面接触,液体表面的油在冷凝板的作用下冷却变成油脂而粘附在冷凝板下面,然后将冷凝板提起,用刮油板将冷凝板下面的油脂刮入到除油槽中,油脂经除油槽下面的油冷冷凝器加热而变成油液,经除油槽底部的出油口流入到接油桶 中。
本发明由于采用上述方法,具有结构新颖,提油效率高,出油纯度高等优点。
Claims (5)
- 一种冷凝式油水分离方法,其特征在于通过油和水的凝固点不同,在油达到凝固点而水并未达到凝固点的温度范围内,实现油和水的高效油液分离.根据权利要求1所述的冷凝式油水分离方法,其特征在于冷凝式油水分离方法通过以下步骤得到:1)、制作冷凝板;2)、对冷凝板进行降温冷凝,使得冷凝板的温度高于水的凝固点而等于或低于油的凝固点;3)、将冷凝后的冷凝板底面放置并接触在静止后的盛有油液的机箱内的液体上表面,将悬浮在液体表面的油冷凝成油脂并粘附到冷凝板上;4)、用刮油板刮除粘附在冷凝板上的油脂。
- 根据权利要求2所述的冷凝式油水分离方法,其特征在于还包括步骤5:对刮除后的除油槽进行加热。
- 根据权利要求2或3所述的冷凝式油水分离方法,其特征在于所述步骤1冷凝板是由平板和冷板蒸发器构成,所述冷板蒸发器固定在平板上,所述冷板蒸发器与热泵系统连接,所述热泵系统与温控开关连接,所述平板是由导温材料制成。
- 根据权利要求3所述的冷凝式油水分离方法,其特征在于所述步骤5除油槽是由槽体和槽体下面的油冷冷凝器构成,所述油冷冷凝器与热泵系统连接。
- 根据权利要求3所述的冷凝式油水分离方法,其特征在于所述温控开关采用PLC控制器。
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CN113483475B (zh) * | 2021-07-09 | 2022-10-28 | 青岛海尔空调器有限总公司 | 室外机的管内油污回收控制方法 |
CN113483477B (zh) * | 2021-07-15 | 2023-09-19 | 青岛海尔空调器有限总公司 | 室外机的管内油污回收控制方法 |
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