CN110218132B - Medicine strip cooling tank - Google Patents
Medicine strip cooling tank Download PDFInfo
- Publication number
- CN110218132B CN110218132B CN201910514726.XA CN201910514726A CN110218132B CN 110218132 B CN110218132 B CN 110218132B CN 201910514726 A CN201910514726 A CN 201910514726A CN 110218132 B CN110218132 B CN 110218132B
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- China
- Prior art keywords
- drain pipe
- tank
- overflow port
- strip cooling
- filter screen
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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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
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C06—EXPLOSIVES; MATCHES
- C06B—EXPLOSIVES OR THERMIC COMPOSITIONS; MANUFACTURE THEREOF; USE OF SINGLE SUBSTANCES AS EXPLOSIVES
- C06B21/00—Apparatus or methods for working-up explosives, e.g. forming, cutting, drying
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D1/00—Devices using naturally cold air or cold water
- F25D1/02—Devices using naturally cold air or cold water using naturally cold water, e.g. household tap water
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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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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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
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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
- C02F2001/007—Processes including a sedimentation step
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Combustion & Propulsion (AREA)
- Removal Of Floating Material (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention relates to the technical field of emulsion explosive production, in particular to a drug strip cooling tank; comprises a tank body, a conveying belt and a drain pipe; the conveying belt is obliquely laid in the pool body, the drain pipe comprises a drain pipe body and an overflow port arranged at the initial end of the drain pipe body, the overflow port is circular, the axial direction of the overflow port is a vertical direction, the distance between the water outlet and the water surface of the pool body is 1-5cm, and the diameter of the water outlet is 3-4 times of that of the drain pipe. The floating scum and floating oil on the inner surface of the pool body can enter the drain pipe through the overflow port in the drainage process of the drain pipe, and the pool body is discharged through the drain pipe, so that the purpose of self-purification of the pool is achieved in the drainage process.
Description
Technical Field
The invention relates to the technical field of emulsion explosive production, in particular to a drug strip cooling tank.
Background
The invention relates to a cooling tank which is a facility for cooling water in the production process of emulsion explosive cartridges. The shallow water cooling pool is used for cooling the circulating water at normal temperature. Cooling cells that produce only weak or no differential wet mass flow in localized cell areas.
When the medicine strip soaks the cooling in medicine strip cooling bath, the medicine strip of partial breakage makes powder flow out, forms dross and oil slick in the pond, because dross and oil slick distribute at random in the cooling bath, the dross of cooling bath aquatic can gather on the conveyer belt, and the collection degree of difficulty is big, makes the cooling bath produce the pollution.
Disclosure of Invention
The technical problem to be solved by the invention is as follows: provides a medical strip cooling tank for effectively cleaning scum and floating oil in the cooling tank.
In order to solve the technical problems, the invention adopts the technical scheme that:
a medicine strip cooling tank comprises a tank body, a conveying belt and a drain pipe;
the conveying belt is obliquely laid in the pool body, the drain pipe comprises a drain pipe body and an overflow port arranged at the initial end of the drain pipe body, the overflow port is circular, the axial direction of the overflow port is a vertical direction, the distance between the water outlet and the water surface of the pool body is 1-5cm, and the diameter of the water outlet is 3-4 times of that of the drain pipe.
The invention has the beneficial effects that: in the structure of the medical strip cooling pond, the drain pipe is laid in the pond body of the medical strip cooling pond, the overflow port with the diameter 3-4 times that of the drain pipe body is arranged at the initial end of the drain pipe, the overflow port is vertically upward and keeps a distance of 1-5cm with the water surface of the pond body, so that floating slag and floating oil floating on the inner surface of the pond body can enter the drain pipe through the overflow port in the drainage process of the drain pipe, and are discharged out of the pond body through the drain pipe, and the purpose of self-cleaning of the pond is achieved in the drainage process.
Drawings
FIG. 1 is a schematic structural view of a drug strip cooling tank according to an embodiment of the present invention;
description of reference numerals:
1. a tank body; 2. a conveyor belt; 31. a drain pipe body; 32. an overflow port; 33. a notch; 4. a drainage ditch; 41. a filter screen; 5. a water inlet pipe; 51. a through hole; 6. a water storage tower.
Detailed Description
In order to explain technical contents, achieved objects, and effects of the present invention in detail, the following description is made with reference to the accompanying drawings in combination with the embodiments.
The most key concept of the invention is as follows: an overflow port with the diameter 3-4 times that of the drain pipe body is arranged at the initial end of the drain pipe, the overflow port is vertically upward and keeps a distance of 1-5cm with the water surface of the pool body, so that floating slag and floating oil floating on the inner surface of the pool body can enter the drain pipe through the overflow port in the drainage process of the drain pipe.
Referring to fig. 1, the invention relates to a drug strip cooling tank, which comprises a tank body 1, a conveyer belt 2 and a drain pipe;
the conveying belt 2 is obliquely laid in the pool body 1, the drain pipe comprises a drain pipe body 31 and an overflow port 32 arranged at the initial end of the drain pipe body 31, the overflow port 32 is circular, the axial direction of the overflow port 32 is a vertical direction, the distance between the water outlet and the water surface of the pool body 1 is 1-5cm, and the diameter of the water outlet is 3-4 times of that of the drain pipe.
In the structure of the medicine strip cooling pond, the drain pipe is laid in the pond body 1 of the medicine strip cooling pond, the overflow port 32 with the diameter being 313-4 times of that of the drain pipe body is arranged at the initial end of the drain pipe, the overflow port 32 is vertically upward and keeps a distance of 1-5cm with the water surface of the pond body 1, so that floating scum and floating oil on the inner surface of the pond body 1 can enter the drain pipe through the overflow port 32 in the drainage process of the drain pipe and are discharged out of the pond body 1 through the drain pipe, and the purpose of self-cleaning of the pond is achieved in the drainage process.
Further, in the above-mentioned medicine strip cooling tank structure, still include escape canal 4, the end connection in escape canal 4 of drain pipe body 31, be equipped with filter screen 41 in the escape canal 4.
As can be seen from the above description, by connecting the drainage ditch 4 to the end of the drainage pipe body 31, and disposing the filter screen 41 in the drainage ditch 4, when the excess water in the tank body 1 flows to the drainage ditch 4 through the drainage pipe, the scum with a large volume can be filtered through the filter screen 41.
Further, in the above structure of the drug strip cooling tank, the filter screen 41 includes a 100-mesh stainless steel filter screen 41 and a 60-mesh stainless steel filter screen 41 which are sequentially arranged along the drainage direction.
Further, among the above-mentioned medicine strip cooling tank structure, still include sedimentation tank and oil interceptor, sedimentation tank connects in escape canal 4, the oil interceptor is connected in sedimentation tank.
As can be seen from the above description, by connecting the sedimentation tank and the oil separation tank downstream of the drainage ditch 4, the wastewater is treated by the sedimentation tank and the oil separation tank, and the scum and the floating oil in the wastewater are removed and then discharged.
Further, in the above structure of the drug strip cooling pool, a notch 33 is provided at a side of the overflow port 32, and the notch 33 faces the conveyor belt 2.
As can be seen from the above description, the gap 33 is disposed on the side of the overflow port 32 facing the conveyor belt 2, which is beneficial to actively suck the floating oil floating slag adhered to the conveyor belt 2 into the overflow port 32 and discharge the floating oil through the drain pipe during the drainage process, thereby further improving the efficiency of discharging floating oil floating slag.
Further, in the above-mentioned medicine strip cooling pond structure, still include water storage tower 6 and inlet tube 5, inlet tube 5 has been laid in the cell body 1, the top of inlet tube 5 is connected in water storage tower 6, the partial interval 5cm that the inlet tube 5 laid in the cell body 1 offers the through-hole 51 that the diameter is 2 cm.
Known by the above-mentioned description, through setting up 6 replacement water pumps of retaining tower, through setting up 6 height at reasonable with retaining tower to reach the water intake pressure of moderate degree, set up the through-hole 51 that the diameter is 2cm through 5cm at the 5 intervals of inlet tube of laying in cell body 1, make the cooling water get into in the cell body 1 through the through-hole 51 of inlet tube 5, make the cooling water get into in the cell body 1 more even, keep the even of temperature in the cell body 1, improve the cooling effect of medicine strip.
Further, in the above-mentioned medicine strip cooling tank structure, the quantity of conveyer belt 2 is 5, conveyer belt 2 sets up in cell body 1 in the crisscross linking in proper order.
Further, in the above structure of the cooling tank for medical strips, the diameter of the drain pipe is 10 cm.
Example 1
A drug strip cooling tank, which comprises a tank body 1, a conveyer belt 2 and a drain pipe; the conveying belt 2 is obliquely laid in the pool body 1, the drain pipe comprises a drain pipe body 31 and an overflow port 32 arranged at the initial end of the drain pipe body 31, the overflow port 32 is circular, the axial direction of the overflow port 32 is a vertical direction, the distance between the water outlet and the water surface of the pool body 1 is 1-5cm, and the diameter of the water outlet is 3-4 times of that of the drain pipe. Still include escape canal 4, the end connection in escape canal 4 of drain pipe body 31, be equipped with filter screen 41 in the escape canal 4. The filter screen 41 comprises a 100-mesh stainless steel filter screen 41 and a 60-mesh stainless steel filter screen 41 which are sequentially arranged along the drainage direction. Still include sedimentation tank and oil interceptor, the sedimentation tank is connected in escape canal 4, the oil interceptor is connected in the sedimentation tank. The lateral part of the overflow opening 32 is provided with a notch 33, and the notch 33 faces the conveying belt 2. Still include water storage tower 6 and inlet tube 5, inlet tube 5 has been laid in the cell body 1, the top of inlet tube 5 is connected in water storage tower 6, the partial interval 5cm that inlet tube 5 laid in cell body 1 offers the through-hole 51 that the diameter is 2 cm. The quantity of conveyer belt 2 is 5, conveyer belt 2 sets up in the cell body 1 in crisscross linking in proper order. The diameter of the drain pipe is 10 cm.
In summary, in the structure of the drug strip cooling tank provided by the invention, the drain pipe is laid in the tank body of the drug strip cooling tank, the overflow port with the diameter 3-4 times that of the drain pipe body is arranged at the initial end of the drain pipe, the overflow port is vertically upward and keeps a distance of 1-5cm from the water surface of the tank body, so that floating slag and floating oil floating on the inner surface of the tank body can enter the drain pipe through the overflow port in the drainage process of the drain pipe and are discharged out of the tank body through the drain pipe, and the purpose of self-cleaning of the tank is achieved in the drainage process. Through the end-to-end connection escape canal at the drain pipe body, set up the filter screen in the escape canal, when unnecessary water passes through drain pipe flow direction escape canal in the cell body, but filter the great dross of volume through the filter screen. Set up the breach through the one side at the overflow mouth towards the conveyer belt, be favorable to at the drainage in-process, initiatively will adhere in the floating oil dross suction overflow mouth of conveyer belt, discharge through the drain pipe, further improve the discharge efficiency of dross floating oil.
The above description is only an embodiment of the present invention, and not intended to limit the scope of the present invention, and all equivalent changes made by using the contents of the present specification and the drawings, or applied directly or indirectly to the related technical fields, are included in the scope of the present invention.
Claims (4)
1. A drug strip cooling tank is characterized by comprising a tank body, a conveying belt and a drain pipe;
the conveying belt is obliquely laid in the pool body, the drain pipe comprises a drain pipe body and an overflow port arranged at the initial end of the drain pipe body, the overflow port is circular, the axial direction of the overflow port is a vertical direction, the distance between the drain port and the water surface of the pool body is 1-5cm, the diameter of the drain port is 3-4 times of that of the drain pipe, and a notch is arranged at the side part of the overflow port and faces the conveying belt;
the tail end of the drain pipe body is connected with the drainage ditch, and a filter screen is arranged in the drainage ditch;
the device also comprises a sedimentation tank and an oil separation tank, wherein the sedimentation tank is connected with the drainage ditch, and the oil separation tank is connected with the sedimentation tank; the diameter of the drain pipe is 10 cm.
2. The drug strip cooling tank of claim 1, wherein the filter screen comprises a 100-mesh stainless steel filter screen and a 60-mesh stainless steel filter screen which are arranged in sequence along the drainage direction.
3. The drug strip cooling tank of claim 1, further comprising a water storage tower and a water inlet pipe, wherein the water inlet pipe is laid in the tank body, the initial end of the water inlet pipe is connected to the water storage tower, and through holes with the diameter of 2cm are formed in the part, laid in the tank body, of the water inlet pipe at intervals of 5 cm.
4. The drug strip cooling pond according to claim 1, wherein the number of the conveying belts is 5, and the conveying belts are sequentially arranged in the pond body in a staggered connection manner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910514726.XA CN110218132B (en) | 2019-06-14 | 2019-06-14 | Medicine strip cooling tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910514726.XA CN110218132B (en) | 2019-06-14 | 2019-06-14 | Medicine strip cooling tank |
Publications (2)
Publication Number | Publication Date |
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CN110218132A CN110218132A (en) | 2019-09-10 |
CN110218132B true CN110218132B (en) | 2021-04-27 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201910514726.XA Active CN110218132B (en) | 2019-06-14 | 2019-06-14 | Medicine strip cooling tank |
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CN (1) | CN110218132B (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB604874A (en) * | 1945-12-07 | 1948-07-12 | Frederick Alexander Ferrier Cr | Improvements in or relating to the continuous manufacture of nitroglycerine and the like explosive liquid nitric esters |
CN201245572Y (en) * | 2008-07-14 | 2009-05-27 | 唐秋明 | Continuous steel belt soaking type cooler with emulsified explosive substrate |
CN202544070U (en) * | 2012-04-10 | 2012-11-21 | 福建省西汉园林景观工程有限公司 | Overflow system for pools |
-
2019
- 2019-06-14 CN CN201910514726.XA patent/CN110218132B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB604874A (en) * | 1945-12-07 | 1948-07-12 | Frederick Alexander Ferrier Cr | Improvements in or relating to the continuous manufacture of nitroglycerine and the like explosive liquid nitric esters |
CN201245572Y (en) * | 2008-07-14 | 2009-05-27 | 唐秋明 | Continuous steel belt soaking type cooler with emulsified explosive substrate |
CN202544070U (en) * | 2012-04-10 | 2012-11-21 | 福建省西汉园林景观工程有限公司 | Overflow system for pools |
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CN110218132A (en) | 2019-09-10 |
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