TWM562851U - Oil and water separation system - Google Patents
Oil and water separation system Download PDFInfo
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- TWM562851U TWM562851U TW107205024U TW107205024U TWM562851U TW M562851 U TWM562851 U TW M562851U TW 107205024 U TW107205024 U TW 107205024U TW 107205024 U TW107205024 U TW 107205024U TW M562851 U TWM562851 U TW M562851U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 162
- 238000000926 separation method Methods 0.000 title claims abstract description 53
- 238000010438 heat treatment Methods 0.000 claims abstract description 11
- 239000002569 water oil cream Substances 0.000 claims description 21
- 239000012530 fluid Substances 0.000 claims description 10
- 238000012544 monitoring process Methods 0.000 claims description 4
- 230000005484 gravity Effects 0.000 claims description 2
- 238000001816 cooling Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 4
- 238000004891 communication Methods 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000009191 jumping Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
一種油水分離系統，包含一儲油槽、至少一第一熱交換器、一超重力分離裝置、一第二熱交換器及一熱泵。該超重力分離裝置連通至該至少一第一熱交換器。該第二熱交換器連通至該超重力分離裝置。該熱泵連通至該至少一第一熱交換器並構成一循環熱水管路，且連通至該第二熱交換器並構成一循環冷水管路，用於從該循環冷水管路吸熱並放熱至該循環熱水管路。該油水分離系統可減少系統供熱及供冷所需的總能量消耗，且能節省系統配置所需的空間。An oil-water separation system comprises an oil storage tank, at least a first heat exchanger, a super-gravity separation device, a second heat exchanger and a heat pump. The supergravity separation device is in communication with the at least one first heat exchanger. The second heat exchanger is in communication with the supergravity separation device. The heat pump is connected to the at least one first heat exchanger and constitutes a circulating hot water line, and is connected to the second heat exchanger and constitutes a circulating cold water line for absorbing heat from the circulating cold water line and releasing the heat to the Circulating hot water line. The oil-water separation system reduces the total energy consumption required for system heating and cooling, and saves space for system configuration.
Description
本新型是有關於一種油水分離系統，特別是指一種包含一熱泵且適用於分離一油水乳化液中的油及水的油水分離系統。The present invention relates to an oil-water separation system, and more particularly to an oil-water separation system comprising a heat pump and suitable for separating oil and water in an oil-water emulsion.
含有油水乳化液的廢液需要經過妥善回收處理以避免污染環境。對於呈現水包油形態的油水乳化液而言，難以透過簡單的靜置(重力)使油水分層而分離油及水，因此需要透過油水分離系統進行處理。Waste liquids containing oil-water emulsions need to be properly recycled to avoid environmental pollution. In the oil-water emulsion which exhibits an oil-in-water form, it is difficult to separate the oil and water by the oily water layer by simple standing (gravity), and therefore it is necessary to carry out treatment by the oil-water separation system.
然而，現有油水分離系統在分離的過程中通常需要添加具有污染風險的破乳劑。若是不添加破乳劑，往往需要分別使用高耗能的熱源設備及冷源設備以提高分離效率，不僅增加了能源消耗的成本，也增加了系統裝置配置所需的空間。However, existing oil-water separation systems typically require the addition of a demulsifier at risk of contamination during the separation process. If the demulsifier is not added, it is often necessary to separately use the high-energy heat source equipment and the cold source equipment to improve the separation efficiency, which not only increases the cost of energy consumption, but also increases the space required for the system device configuration.
因此，本新型之目的，即在提供一種油水分離系統，可以克服上述先前技術的缺點。Accordingly, it is an object of the present invention to provide a water-oil separation system that overcomes the disadvantages of the prior art described above.
於是，本新型油水分離系統適用於分離一油水乳化液中的油及水，該油水分離系統包含一儲油槽、至少一第一熱交換器、一超重力分離裝置、一第二熱交換器及一熱泵。該儲油槽用於儲存該油水乳化液。該至少一第一熱交換器用於加熱該儲油槽內的油水乳化液。該超重力分離裝置連通至該至少一第一熱交換器，用於透過離心力及真空環境從經該至少一第一熱交換器加熱後的油水乳化液中分離出油及水氣。該第二熱交換器連通至該超重力分離裝置，用於冷凝該水氣以形成冷凝水。該熱泵連通至該至少一第一熱交換器並構成一循環熱水管路，且連通至該第二熱交換器並構成一循環冷水管路，用於從該循環冷水管路吸熱並放熱至該循環熱水管路。Therefore, the novel oil-water separation system is suitable for separating oil and water in an oil-water emulsion, the oil-water separation system comprising an oil storage tank, at least a first heat exchanger, a super-gravity separation device, a second heat exchanger and A heat pump. The oil storage tank is used to store the oil-water emulsion. The at least one first heat exchanger is for heating the oil-water emulsion in the oil storage tank. The supergravity separation device is connected to the at least one first heat exchanger for separating oil and moisture from the oil-water emulsion heated by the at least one first heat exchanger through a centrifugal force and a vacuum environment. The second heat exchanger is in communication with the supergravity separation device for condensing the moisture to form condensed water. The heat pump is connected to the at least one first heat exchanger and constitutes a circulating hot water line, and is connected to the second heat exchanger and constitutes a circulating cold water line for absorbing heat from the circulating cold water line and releasing the heat to the Circulating hot water line.
本新型之功效在於：該油水分離系統可有效減少系統供熱及供冷所需的能源消耗，且能節省系統裝置配置所需的空間。The effect of the novel is that the oil-water separation system can effectively reduce the energy consumption required for system heating and cooling, and can save space required for system device configuration.
以下將就本新型內容進行詳細說明：The following is a detailed description of this new content:
較佳地，該至少一第一熱交換器設置於該儲油槽內，用於加熱該儲油槽內的油水乳化液。Preferably, the at least one first heat exchanger is disposed in the oil storage tank for heating the oil-water emulsion in the oil storage tank.
較佳地，該油水分離系統還包含一熱水槽及一熱水泵，皆設置於該循環熱水管路，該熱水槽用於提供並儲存該循環熱水管路中的流體，該熱水泵用於控制該循環熱水管路中流體的流向。Preferably, the oil-water separation system further comprises a hot water tank and a hot water pump, which are disposed in the circulating hot water pipeline, wherein the hot water tank is used for providing and storing the fluid in the circulating hot water pipeline, and the hot water pump is used for controlling The flow direction of the fluid in the circulating hot water line.
較佳地，該油水分離系統還包含一冷水槽及一冷水泵，皆設置於該循環冷水管路，該冷水槽用於提供並儲存該循環冷水管路中的流體，該冷水泵用於控制該循環冷水管路中流體的流向。Preferably, the oil-water separation system further comprises a cold water tank and a cold water pump, which are all disposed in the circulating cold water pipeline, wherein the cold water tank is used for providing and storing the fluid in the circulating cold water pipeline, and the cold water pump is used for controlling The flow direction of the fluid in the circulating cold water line.
較佳地，該儲油槽設置於該超重力分離裝置下方，用於接收該油，以使該油與該油水乳化液混合。Preferably, the oil reservoir is disposed below the supergravity separation device for receiving the oil to mix the oil with the oil-water emulsion.
較佳地，該油水分離系統還包含一冷凝水接收槽，連通至該第二熱交換器且設置於該第二熱交換器下方，用於收集該冷凝水。Preferably, the oil-water separation system further comprises a condensate receiving tank connected to the second heat exchanger and disposed under the second heat exchanger for collecting the condensed water.
更佳地，該熱水槽、該熱水泵及該熱泵是依序並列設置，且鄰近設置於該至少一第一熱交換器。More preferably, the hot water tank, the hot water pump and the heat pump are arranged side by side and arranged adjacent to the at least one first heat exchanger.
更佳地，該冷水槽、該冷水泵及該熱泵是依序並列設置，且鄰近設置於該第二熱交換器。More preferably, the cold water tank, the cold water pump and the heat pump are arranged side by side and disposed adjacent to the second heat exchanger.
更佳地，該油水分離系統還包含一真空泵，連通至該冷凝水接收槽，以使該冷凝水接收槽、該第二熱交換器、該超重力分離裝置及該儲油槽的內部呈負壓。該負壓能使該超重力分離裝置中的水較容易汽化分離。More preferably, the oil-water separation system further comprises a vacuum pump connected to the condensate receiving tank, so that the condensed water receiving tank, the second heat exchanger, the super-gravity separating device and the inside of the oil storage tank are under negative pressure . The negative pressure enables the water in the supergravity separation device to be more easily vaporized and separated.
更佳地，該油水分離系統還包含一電控裝置，用於監控該循環熱水管路及該循環冷水管路內的溫度，以避免該熱泵因入水溫度過高或過低而自動跳機，並用於監控該冷凝水接收槽、該第二熱交換器、該超重力分離裝置及該儲油槽內部的壓力。More preferably, the oil-water separation system further comprises an electric control device for monitoring the temperature of the circulating hot water pipe and the circulating cold water pipe to prevent the heat pump from automatically jumping due to the inlet water temperature being too high or too low. And for monitoring the condensate receiving tank, the second heat exchanger, the supergravity separating device and the pressure inside the oil sump.
在本新型被詳細描述之前，應當注意在以下的說明內容中，類似的元件是以相同的編號來表示。Before the present invention is described in detail, it should be noted that in the following description, similar elements are denoted by the same reference numerals.
本新型將就以下實施例來作進一步說明，但應瞭解的是，該實施例僅為例示說明之用，而不應被解釋為本新型實施之限制。The present invention will be further described in the following examples, but it should be understood that this embodiment is intended to be illustrative only and not to be construed as limiting.
參閱圖1與圖2，本新型油水分離系統100之一實施例適用於分離一油水乳化液中的油及水，該油水分離系統100包含一儲油槽1、三個第一熱交換器2、一超重力分離裝置3、一第二熱交換器4、一熱水槽5、一熱水泵52、一冷水槽6、一冷水泵62、一熱泵7、一冷凝水接收槽8、一真空泵81及一電控裝置9。Referring to FIG. 1 and FIG. 2, an embodiment of the novel oil-water separation system 100 is suitable for separating oil and water in an oil-water emulsion, and the oil-water separation system 100 includes an oil storage tank 1, three first heat exchangers 2. a super-gravity separation device 3, a second heat exchanger 4, a hot water tank 5, a hot water pump 52, a cold water tank 6, a cold water pump 62, a heat pump 7, a condensed water receiving tank 8, a vacuum pump 81, and An electronic control device 9.
該儲油槽1設置於該超重力分離裝置3下方，用於儲存該油水乳化液，並用於接收該超重力分離裝置3分離出的油，以使該油與該油水乳化液混合。The oil storage tank 1 is disposed below the super-gravity separation device 3 for storing the oil-water emulsion and for receiving the oil separated by the super-gravity separation device 3 to mix the oil with the oil-water emulsion.
該等第一熱交換器2設置於該儲油槽1內，用於加熱該儲油槽1內的油水乳化液。The first heat exchanger 2 is disposed in the oil storage tank 1 for heating the oil-water emulsion in the oil storage tank 1.
該超重力分離裝置3連通至該儲油槽1，用於透過離心力及真空環境從該油水乳化液中分離出油及水氣。The supergravity separation device 3 is connected to the oil storage tank 1 for separating oil and moisture from the oil-water emulsion through a centrifugal force and a vacuum environment.
該第二熱交換器4連通至該超重力分離裝置3，用於冷凝該超重力分離裝置3分離出的水氣以形成冷凝水。The second heat exchanger 4 is connected to the supergravity separation device 3 for condensing the moisture separated by the supergravity separation device 3 to form condensed water.
該熱泵7連通至該等第一熱交換器2並構成一循環熱水管路51(如圖1及圖2中的細線箭頭所示)，且連通至該第二熱交換器4並構成一循環冷水管路61(如圖1及圖2中的粗線箭頭所示)，用於從該循環冷水管路61吸熱並放熱至該循環熱水管路51，以進一步加熱來自於該熱水槽5的熱水並冷卻來自於該冷水槽6的冷水。The heat pump 7 is connected to the first heat exchangers 2 and constitutes a circulating hot water line 51 (shown by thin arrow in FIGS. 1 and 2), and communicates to the second heat exchanger 4 and constitutes a cycle. a cold water line 61 (shown by thick arrows in FIGS. 1 and 2) for absorbing heat from the circulating cold water line 61 and radiating heat to the circulating hot water line 51 for further heating from the hot water tank 5. The hot water is cooled and the cold water from the cold water tank 6 is cooled.
該熱水槽5連通至該等第一熱交換器2並設置於該循環熱水管路51，用於提供並儲存該循環熱水管路51中的熱水。該熱水泵52設置於該循環熱水管路51，用於控制該循環熱水管路51中流體的流向。該熱水槽5、該熱水泵52及該熱泵7是依序並列設置，且鄰近設置於該等第一熱交換器2。在本實施例的操作中，該熱水槽5中的熱水經由該熱水泵52打出至該熱泵7中進一步加熱，再流入該儲油槽1內的第一熱交換器2，以供應該等第一熱交換器2加熱該儲油槽1內的油水乳化液，隨後循環回到該熱水槽5中。The hot water tank 5 is connected to the first heat exchangers 2 and disposed in the circulating hot water line 51 for supplying and storing hot water in the circulating hot water line 51. The hot water pump 52 is disposed in the circulating hot water line 51 for controlling the flow direction of the fluid in the circulating hot water line 51. The hot water tank 5, the hot water pump 52, and the heat pump 7 are arranged in parallel, and are disposed adjacent to the first heat exchangers 2. In the operation of the embodiment, the hot water in the hot water tank 5 is discharged to the heat pump 7 via the hot water pump 52 for further heating, and then flows into the first heat exchanger 2 in the oil storage tank 1 to supply the first A heat exchanger 2 heats the oil-water emulsion in the oil sump 1 and then circulates back into the hot water tank 5.
該冷水槽6連通至該第二熱交換器4並設置於該循環冷水管路61，用於提供並儲存該循環冷水管路61中的冷水。該冷水泵62設置於該循環冷水管路61，用於控制該循環冷水管路61中流體的流向。該冷水槽6、該冷水泵62及該熱泵7是依序並列設置，且鄰近設置於該第二熱交換器4。在本實施例的操作中，該冷水槽6中的冷水經由該冷水泵62打出至該熱泵7中進一步冷卻，再流入該第二熱交換器4，以供應該第二熱交換器4冷凝該水氣以形成冷凝水，隨後循環回到該冷水槽6中。The cold water tank 6 is connected to the second heat exchanger 4 and disposed in the circulating cold water line 61 for supplying and storing cold water in the circulating cold water line 61. The chilled water pump 62 is disposed in the circulating cold water line 61 for controlling the flow direction of the fluid in the circulating cold water line 61. The cold water tank 6, the chill water pump 62, and the heat pump 7 are arranged in parallel, and are disposed adjacent to the second heat exchanger 4. In the operation of the embodiment, the cold water in the cold water tank 6 is discharged to the heat pump 7 through the cold water pump 62 for further cooling, and then flows into the second heat exchanger 4 to supply the second heat exchanger 4 to condense the The water vapor forms condensed water and is then recycled back to the cold water tank 6.
該冷凝水接收槽8連通至該第二熱交換器4且設置於該第二熱交換器4下方，用於收集該冷凝水。The condensed water receiving tank 8 is connected to the second heat exchanger 4 and disposed below the second heat exchanger 4 for collecting the condensed water.
該真空泵81連通至該冷凝水接收槽8，以使該冷凝水接收槽8、該第二熱交換器4、該超重力分離裝置3及該儲油槽1的內部呈負壓。The vacuum pump 81 is connected to the condensed water receiving tank 8 such that the condensed water receiving tank 8, the second heat exchanger 4, the supergravity separating apparatus 3, and the inside of the oil sump 1 are under a negative pressure.
該電控裝置9用於監控該循環熱水管路51內的熱水溫度及該循環冷水管路61內的冷水溫度，並用於監控該冷凝水接收槽8、該第二熱交換器4、該超重力分離裝置3及該儲油槽1內部的壓力。The electronic control device 9 is configured to monitor the temperature of the hot water in the circulating hot water line 51 and the temperature of the cold water in the circulating cold water line 61, and monitor the condensed water receiving tank 8, the second heat exchanger 4, and the The supergravity separation device 3 and the pressure inside the oil storage tank 1.
綜上所述，本新型油水分離系統100藉由設置於該循環熱水管路51及該循環冷水管路61的熱泵7，從該循環冷水管路61吸熱並放熱至該循環熱水管路51，有效運用熱能轉移作為供應加熱該油水乳化液的熱源並作為供應冷凝該水氣的冷源，可有效減少系統供熱及供冷所需的能源消耗，且能節省系統裝置配置所需的空間，故確實能達成本新型之目的。In summary, the new oil-water separation system 100 absorbs heat from the circulating cold water pipe 61 and radiates heat to the circulating hot water pipe 51 by the heat pump 7 disposed in the circulating hot water pipe 51 and the circulating cold water pipe 61. The effective use of thermal energy transfer as a heat source for heating the oil-water emulsion and as a cold source for supplying the water vapor can effectively reduce the energy consumption required for system heating and cooling, and can save space required for system device configuration. Therefore, the purpose of this new type can be achieved.
惟以上所述者，僅為本新型之實施例而已，當不能以此限定本新型實施之範圍，凡是依本新型申請專利範圍及專利說明書內容所作之簡單的等效變化與修飾，皆仍屬本新型專利涵蓋之範圍內。However, the above is only the embodiment of the present invention, and when it is not possible to limit the scope of the present invention, all the simple equivalent changes and modifications according to the scope of the patent application and the contents of the patent specification are still This new patent covers the scope.
100‧‧‧油水分離系統
1‧‧‧儲油槽
2‧‧‧第一熱交換器
3‧‧‧超重力分離裝置
4‧‧‧第二熱交換器
5‧‧‧熱水槽
51‧‧‧循環熱水管路
52‧‧‧熱水泵
6‧‧‧冷水槽
61‧‧‧循環冷水管路
62‧‧‧冷水泵
7‧‧‧熱泵
8‧‧‧冷凝水接收槽
81‧‧‧真空泵
9‧‧‧電控裝置100‧‧‧ Oil-water separation system
1‧‧‧ oil storage tank
2‧‧‧First heat exchanger
3‧‧‧Supergravity separation device
4‧‧‧second heat exchanger
5‧‧‧ hot water tank
51‧‧‧Circulating hot water pipeline
52‧‧‧Hot water pump
6‧‧‧ cold sink
61‧‧‧Circular cold water pipeline
62‧‧‧ chilled water pump
7‧‧‧ heat pump
8‧‧‧Condensate receiving tank
81‧‧‧Vacuum pump
9‧‧‧Electric control device
本新型之其他的特徵及功效，將於參照圖式的實施方式中清楚地呈現，其中： ［圖1］是本新型油水分離系統的一實施例的一側視架構示意圖；及 ［圖2］是該實施例的一俯視架構示意圖。Other features and effects of the present invention will be apparent from the following description of the drawings, wherein: FIG. 1 is a side view schematic view of an embodiment of the novel oil-water separation system; and [FIG. 2] It is a schematic top view of the embodiment.
Claims (10)
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| TW107205024U TWM562851U (en) | 2018-04-18 | 2018-04-18 | Oil and water separation system |
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| TW107205024U TWM562851U (en) | 2018-04-18 | 2018-04-18 | Oil and water separation system |
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| TWM562851U true TWM562851U (en) | 2018-07-01 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI897524B (en) * | 2024-07-08 | 2025-09-11 | 黃建嘉 | Oil-water separation system |
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2018
- 2018-04-18 TW TW107205024U patent/TWM562851U/en unknown
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI897524B (en) * | 2024-07-08 | 2025-09-11 | 黃建嘉 | Oil-water separation system |
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