CN210595622U - Green ship ballast water treatment system - Google Patents
Green ship ballast water treatment system Download PDFInfo
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- CN210595622U CN210595622U CN201921627331.2U CN201921627331U CN210595622U CN 210595622 U CN210595622 U CN 210595622U CN 201921627331 U CN201921627331 U CN 201921627331U CN 210595622 U CN210595622 U CN 210595622U
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Abstract
The utility model relates to a green ship ballast water processing system, including tail point ballast water tank, filter electrolytic device, ballast water house steward, sweep cabin water house steward, fire main, ballast sweep cabin jet pump, sweep cabin water house steward, ballast sweep cabin discharge tube, electrolysis water injection pipe, ballast water discharge tube, ballast discharge flowmeter, ballast conveyer pipe, ballast self priming pump, ballast sea water tank, its simple structure is reasonable, can satisfy the ballast water and load the emission according to the region requirement, is favorable to the boats and ships environmental protection, steady operation.
Description
Technical Field
The utility model relates to a ship system, a green ship ballast water processing system specifically says so.
Background
The development of the shipping industry at any time has higher and higher requirements on energy conservation and environmental protection of ships. Wherein the emission of marine sulfides is an important source for global environmental pollution, and 65-70% of suspended particulate matters (PM2.5) and sulfur oxides come from ships worldwide. The sulfide is generated by fuel oil with high sulfur content, and the sulfide in the waste gas can be dissolved in water to form acid rain, thus destroying crops, soil and fresh water resources and having great harm to the environment and human health.
Further, the cargo ships have different displacement amounts when loading and unloading cargo, and ballast water is loaded and discharged according to the ship loading state during navigation in order to ensure safe ship travel. However, different loading and discharge locations can cause microbial intrusion and contamination problems. For example, a cargo ship sailing from the sea and traveling to the united states will carry microbes from the sea to the united states. As countries frequently transport goods, the risk is increasing.
Disclosure of Invention
The utility model provides a rational in infrastructure, the ballast water is loaded according to the regional requirement and is discharged, is favorable to the green ship ballast water processing system of boats and ships environmental protection, steady operation.
The utility model adopts the technical proposal that: a green environmental protection ship ballast water treatment system comprises a tail tip ballast water tank, a filtering electrolysis device, a main ballast water pipe, a main scavenging water pipe, a main fire-fighting pipe, a ballast scavenging jet pump, a main scavenging water pipe, a ballast scavenging discharge pipe and an electrolyzed water injection pipe, the ballast water discharge pipe, the ballast discharge flowmeter, the ballast conveying pipe, the ballast self-priming pump, the ballast sea water tank, the fire main pipe, the main water pipe for the scavenging tank, the ballast scavenging tank discharge pipe are connected with the ballast scavenging jet pump, the ballast water main pipe is divided into two paths, one path is connected with the ballast water discharge pipe with a valve after being connected with the electrolytic water injection pipe, the other path is connected with the ballast sea water tank through the ballast injection pipe with the valve and is connected with the ballast self-priming pipe in a branch path, the ballast self-priming pipe is provided with the ballast self-priming pump and the filtering electrolysis device, and the ballast self-priming pipe is connected with the ballast water discharge pipe with; the ballast water main pipe is also connected to a tail tip ballast water tank through a valve, and the tail tip ballast water tank is connected to the filtering electrolysis device through the valve; the filtering electrolysis device comprises an electrolysis input pipe, a ballast filter, a fresh water inlet pipe, a filtration backflushing discharge pipe, an electrolysis booster pump, an electrolysis steam heater, an electrolysis unit and an electrolysis output pipe, wherein a tail tip ballast water tank is connected with the electrolysis input pipe through a valve, the electrolysis input pipe is divided into two paths and is respectively connected with a backflushing part of the ballast filter and the electrolysis booster pump through the valve, the backflushing part of the ballast filter is connected with the external discharge through the filtration backflushing discharge pipe, the filtering part of the ballast filter is connected with a ballast self-sucking pump on the ballast self-sucking pipe through the ballast filter pipe, the ballast filter pipe is connected with the fresh water inlet pipe, the electrolysis booster pump is connected with the electrolysis steam heater, the electrolysis steam heater is connected with the electrolysis unit, the electrolysis output pipe is.
Further, the electrolysis steam heater is connected with the cabin steam system and the cabin condensate system.
Furthermore, valves are arranged in the front and the back of each pipeline junction point and on two sides of each pump.
Furthermore, a sampling port and a neutralization port are arranged on the ballast water main pipe, sampling ports are arranged on the ballast scavenging tank discharge pipe and the ballast water discharge pipe, the sampling ports are connected with a sampling unit, the sampling unit is divided into two paths and respectively connected with a detection unit and an inlet of a ballast self-sucking pump, the detection unit is connected with a sampling tank, and the sampling tank is connected with the inlet of the ballast self-sucking pump through a pump; the fresh water inlet pipe is also connected with a neutralization port through a valve.
The utility model discloses ballast water processing system, the fresh water that adopts no chlorine or low chlorine that tail point ballast water cabin stores in the fresh water region is as the electrolysis source, the ballast water house steward divide into about according to boats and ships about ballast water house steward, the last valve of ballast filling tube is opened, two ballast water house steward send ballast water respectively or simultaneously as required, the last valve of ballast self-priming pipe and ballast water discharge tube is closed, ballast water directly sends to two ballast sea water tanks about to, ballast sea water tank establishes the filter in front and filters, point ballast water cabin send water to filter electrolytic device this moment, via the electrolysis input tube, the electrolysis booster pump, electrolysis steam heater is electrolytic in electrolytic cell, the electrolysis water is sent to ballast sea water tank through the electrolysis water filling tube through the electrolysis output tube, can effectively eliminate the microorganism in the different sea area invading ballast water, reach the risk that reduces the organism; when ballast water needs to be discharged, the upper valve of the ballast injection pipe is closed, the upper valves of the ballast self-sucking pipe and the ballast water discharge pipe are opened, ballast water on the ballast sea water tank is sucked by the ballast self-sucking pump, the ballast water discharge pipe is connected with the ballast water discharge pipe by the ballast discharge flowmeter, a sampling port is formed in the ballast water discharge pipe, a sample is sent to the sampling unit, the sampling unit is directly connected with return liquid at the inlet of the ballast self-sucking pump or is connected with the inlet of the ballast self-sucking pump by a pump through a sampling tank, if the sample is qualified, the valve on the ballast self-sucking pipe in parallel connection with the ballast filter pipe is opened, the upper valve of the ballast filter tank is closed, the ballast water is directly discharged, if the sample is unqualified, the valve on the ballast self-sucking pipe in parallel connection with the ballast filter pipe is closed, the upper valve on the ballast filter tank is opened, ballast crystal ballast self-, suspended particles in ballast water in different sea areas can be effectively filtered, and the risk of biological invasion is reduced; after the ballast water is discharged, residual ballast water in tanks and pipes in the ballast system needs to be removed, related pipeline valves are opened, and a ballast scavenging injection pump is started to suck the residual ballast water in the ballast water main pipe, the ballast self-sucking pipe, the ballast injection pipe and the ballast seawater tank through a fire main pipe and a scavenging water main pipe, so that the pipeline sanitation and the pipeline safety life are effectively ensured.
Drawings
FIG. 1 is a diagram of a ballast water treatment system according to the present invention;
FIG. 2 is a diagram of a filtration and electrolysis apparatus of the ballast water treatment system of the present invention;
fig. 3 is a sampling system diagram of the ballast water treatment system of the present invention.
In the figure: the ballast water main pipe 19, the main scavenge water pipe 20, the fire main pipe 21, the ballast scavenge jet pump 22, the ballast scavenge port discharge pipe 23, the electrolytic water injection pipe 24, the ballast water discharge pipe 25, the ballast injection pipe 26, the ballast sea water tank 27, the ballast injection filter 28, the ballast self-suction pipe 29, the ballast sampling return port 30, the ballast self-suction pump 31, the ballast filtration switching valve 32, the ballast discharge flowmeter 33, the filtration and electrolysis apparatus 34, the electrolysis input pipe 35, the ballast filtration pipe 36, the ballast filter 37, the fresh water inlet pipe 38, the filtration discharge pipe 39, the electrolysis booster pump 40, the electrolysis steam heater 41, the electrolysis unit 42, the electrolysis injection pump 43, the electrolysis output pipe 44, the neutralization port 45, the sampling port 46, the tail tip ballast tank 75, the sampling unit 48, the sampling tank 49, the sampling return pump 50, and the sampling return pipe 51.
Detailed Description
The present invention will be further explained with reference to the drawings and examples.
1-3, the ballast water treatment system comprises a ballast water main pipe 19, a scavenging water main pipe 20, a fire main pipe 21, a ballast scavenging jet pump 22, a ballast scavenging discharge pipe 23, an electrolytic water injection pipe 24, a ballast water discharge pipe 25, a ballast injection pipe 26, a ballast seawater tank 27, a ballast injection filter 28, a ballast self-sucking pipe 29, a ballast sampling liquid return port 30, a ballast self-sucking pump 31, a ballast filtering switching valve 32, a ballast discharge flowmeter 33, a filtering electrolysis device 34, an electrolysis input pipe 35, a ballast filtering pipe 36, a ballast filter 37, a fresh water inlet pipe 38, a filtering back-flushing discharge pipe 39, an electrolysis booster pump 40, an electrolysis steam heater 41, an electrolysis unit 42, an electrolysis injection pump 43, an electrolysis output pipe 44, a neutralization port 45, a sampling port 46, a tail tip ballast water tank 75, a sampling unit 48, a sampling tank 49, a tail tip ballast water tank 45, a sampling unit 48, a sampling tank 49, a water tank, A sample return pump 50 and a sample return pipe 51. In the embodiment, the ballast water system adopts a left ballast seawater cabin and a right ballast seawater cabin which are matched with a left ballast water main pipe and a right ballast water main pipe for supplying, the following detailed description is given by using a single line (which can be explained and understood by referring to the drawings), the fire main pipe 21, the scavenging water main pipe 20 and the ballast scavenging discharge pipe 23 are connected with the ballast scavenging jet pump 22, each of the left and right ballast main pipes 19 is divided into 5 lines, the first line is connected with the ballast water discharge pipe 25 with a valve after being connected with the electrolytic water injection pipe 24, the other 4 lines are divided into two same lines, each line is connected with the ballast sea water tank 27 corresponding to the ballast main pipe with a valve through the ballast injection pipe 26 with a valve and is connected with the ballast self-sucking pipe 29 by branch, the ballast self-sucking pipe 29 is sequentially provided with a ballast sampling liquid return port 30, a ballast self-sucking pump 31, a ballast filtering switching valve 32 and a ballast discharge flowmeter 33 and is connected with the ballast water discharge pipe 25, and the ballast filtering electrolysis device 34 is connected with the ballast filtering switching valve; the ballast water main pipe 19 is also connected to a tail tip ballast water tank 75 through a valve, and the tail tip ballast water tank is connected to the filtering electrolysis device 34 through the valve; as shown in fig. 3, the filtration and electrolysis device comprises an electrolysis input pipe 35, a ballast filter pipe 36, a ballast filter 37, a fresh water inlet pipe 38, a filtration recoil discharge pipe 39, an electrolysis booster pump 40, an electrolysis steam heater 41, an electrolysis unit 42, an electrolysis injection pump 43 and an electrolysis output pipe 44, a tail tip ballast water tank 75 is connected with the electrolysis input pipe 35 through a valve, the electrolysis input pipe 35 is connected with a recoil part of the ballast filter 37 and the electrolysis booster pump 40 through valves respectively in two ways, the recoil part of the ballast filter is connected with external discharge through the filtration recoil discharge pipe 39, the filtration part of the ballast filter 37 is connected with a ballast self-priming pump on a ballast pipe through the ballast filter pipe 36, the filtration pipe is connected with the fresh water inlet pipe 38, the electrolysis booster pump 40 is connected with the electrolysis steam heater 41, the electrolysis steam heater is connected with the electrolysis unit 42, the electrolysis unit is connected with the electrolysis output pipe 44 with the, the electrolysis output pipe is connected with an electrolysis water injection pipe 24; the ballast water main pipe is provided with a sampling port 46 and a neutralization port 45, the ballast scavenging tank discharge pipe and the ballast water discharge pipe are provided with sampling ports, the sampling ports are connected with a sampling unit 47, the sampling unit is divided into two paths and respectively connected with a detection unit 48 and a ballast sampling liquid return port 30 through a sampling liquid return pipe 51, the detection unit is connected with a sampling tank 49, and the sampling tank is connected with the ballast sampling liquid return port 30 through a sampling liquid return pump 50; the fresh water inlet pipe is also connected with a neutralization port through a valve.
On the basis of the embodiment, the electrolytic steam heater is connected with a cabin steam system and a cabin condensate system. The valve is all had around each pipeline cross connection point, each pump both sides to and each valve on each pipe, the cabin sets up as required, and switching control is the prior art of pipeline valve accuse, the utility model discloses do not do detailed description.
Claims (4)
1. A green environmental protection ship ballast water processing system which characterized in that:
the ballast water self-priming device comprises a tail tip ballast water tank, a filtering electrolysis device, a ballast water main pipe, a scavenging water main pipe, a fire main pipe, a ballast scavenging injection pump, a scavenging water main pipe, a ballast scavenging discharge pipe, an electrolysis water injection pipe, a ballast water discharge pipe, a ballast discharge flowmeter, a ballast conveying pipe, a ballast self-priming pump, a ballast sea water tank, a fire main pipe, a scavenging water main pipe and a ballast scavenging discharge pipe are connected with the ballast scavenging injection pump, the ballast water main pipe is divided into two paths, one path is connected with the ballast water discharge pipe with a valve after being connected with the electrolysis water injection pipe, the other path is connected with the ballast water self-priming tank and the ballast pipe by a branch through the ballast injection pipe with a valve, the ballast self-priming pump and the filtering electrolysis device are arranged on the ballast self-priming pipe, and the ballast water discharge pipe with the valve is; the ballast water main pipe is also connected to a tail tip ballast water tank through a valve, and the tail tip ballast water tank is connected to the filtering electrolysis device through the valve; the filtering electrolysis device comprises an electrolysis input pipe, a ballast filter, a fresh water inlet pipe, a filtration backflushing discharge pipe, an electrolysis booster pump, an electrolysis steam heater, an electrolysis unit and an electrolysis output pipe, wherein a tail tip ballast water tank is connected with the electrolysis input pipe through a valve, the electrolysis input pipe is divided into two paths and is respectively connected with a backflushing part of the ballast filter and the electrolysis booster pump through the valve, the backflushing part of the ballast filter is connected with the external discharge through the filtration backflushing discharge pipe, the filtering part of the ballast filter is connected with a ballast self-sucking pump on the ballast self-sucking pipe through the ballast filter pipe, the ballast filter pipe is connected with the fresh water inlet pipe, the electrolysis booster pump is connected with the electrolysis steam heater, the electrolysis steam heater is connected with the electrolysis unit, the electrolysis output pipe is.
2. The green environmental-friendly ship ballast water treatment system as claimed in claim 1, wherein: the electrolytic steam heater is connected with the cabin steam system and the cabin condensate system.
3. The green environmental-friendly ship ballast water treatment system as claimed in claim 1, wherein: valves are arranged at the front and the back of each pipeline joint point and at the two sides of each pump.
4. The green environmental-friendly ship ballast water treatment system as claimed in claim 1, wherein: the ballast water main pipe is provided with a sampling port and a neutralization port, the ballast scavenging tank discharge pipe and the ballast water discharge pipe are provided with sampling ports, the sampling ports are connected with a sampling unit, the sampling unit is divided into two paths and respectively connected with a detection unit and a ballast self-sucking pump inlet, the detection unit is connected with a sampling tank, and the sampling tank is connected with the ballast self-sucking pump inlet through a pump; the fresh water inlet pipe is also connected with a neutralization port through a valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921627331.2U CN210595622U (en) | 2019-09-25 | 2019-09-25 | Green ship ballast water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921627331.2U CN210595622U (en) | 2019-09-25 | 2019-09-25 | Green ship ballast water treatment system |
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| CN210595622U true CN210595622U (en) | 2020-05-22 |
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| CN201921627331.2U Active CN210595622U (en) | 2019-09-25 | 2019-09-25 | Green ship ballast water treatment system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110467294A (en) * | 2019-09-25 | 2019-11-19 | 江苏扬子鑫福造船有限公司 | A kind of environmentally protective ship ballast water treatment system |
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2019
- 2019-09-25 CN CN201921627331.2U patent/CN210595622U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110467294A (en) * | 2019-09-25 | 2019-11-19 | 江苏扬子鑫福造船有限公司 | A kind of environmentally protective ship ballast water treatment system |
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