CN204939590U - A kind of with water cycle cooling mercury vapour device - Google Patents
A kind of with water cycle cooling mercury vapour device Download PDFInfo
- Publication number
- CN204939590U CN204939590U CN201520721481.5U CN201520721481U CN204939590U CN 204939590 U CN204939590 U CN 204939590U CN 201520721481 U CN201520721481 U CN 201520721481U CN 204939590 U CN204939590 U CN 204939590U
- Authority
- CN
- China
- Prior art keywords
- cooling tower
- cooling
- water
- tower
- outlet
- Prior art date
- 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.)
- Expired - Fee Related
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model relates to mercury vapour cooling technology field, especially a kind of with water cycle cooling mercury vapour device, by improving the structure of refrigerating unit, make device by casing, be arranged on the cooling tower on casing, be arranged on the import on body side and be arranged on and form with the outlet arranged on the diagonally opposing corner of import opposite flank, and then make mercury vapour can realize water cycle cooling, and then make the duration of contact of water and steam longer, heat exchange degree is darker, and by the appropriate design to device, and then make the inner sheathed vapour stream siphunculus of water-cooled tube, and then mercury vapour to be leaked in environment and to pollute the probability of corrosion cooling tower outer wall lower, and then reduce the emission rate of mercury vapour, reduce environmental pollution rate, improve the cooling performance of mercuryvapour.
Description
Technical field
The utility model relates to mercury vapour cooling technology field, especially a kind of with water cycle cooling mercury vapour device.
Background technology
Mercury is the material that corrodibility is stronger, it can cause corrosion to metals such as cast irons, and then in the process of production and preparation mercury, equipment requirements for mercury is comparatively strict, a large amount of cast iron and metal product is made all to be difficult to as the equipment in mercury production process, even if use thickness to reach equipment that the steel pipe of tens cm thicks and steel board prepared as equipment starting material is to carry out production and the process of mercury, also can in long-term production process, this equipment is caused to be corroded sky, and then the environment produced is threatened, also make the work-ing life of equipment shorter simultaneously, cost prepared by mercury is higher.Especially the equipment reclaimed after liquid being cooled to by the mode that water cycle cools by mercury to the mercuryvapour in production process or device, when it adopts the metals such as cast iron to be prepared to form, its radiating effect is more excellent, rate of heat exchange is higher, but, mercuryvapour will be caused to cause corrosion empty to equipment for the corrosion that mercury is long-term, after mercury is mixed with water, cause water pollution; Mercury vapour is leaked to after in environment, causes the pollution of the environment such as air, and the rate of recovery simultaneously still obtaining mercury is lower, increases the cost recovery of mercury.
For this reason, this investigator combines production practice for many years and the material that adopts heat-exchange equipment of the prior art and heat-exchange equipment and structure are studied and explored, and then adopt the device of water cycle cooling process to improve for mercuryvapour, and then make its structure simple, life cycle is extended, radiating effect is device preferably, and then for providing new departure by water cycle cooling mercury vapour technical field.
Utility model content
In order to solve the above-mentioned technical problem existed in prior art, the utility model provides one water cycle to cool mercury vapour device.
Be achieved particular by following technical scheme:
One water cycle cooling mercury vapour device, by casing, is arranged on the cooling tower on casing, is arranged on the import on body side and is arranged on to form with the outlet arranged on the diagonally opposing corner of import opposite flank.
Described cooling tower is made up of left cooling tower and right cooling tower.
Described import is made up of cooling water outlet and steam inlet, and wherein, steam inlet is enclosed within cooling water outlet.
Distance between the pipe outer wall of described steam inlet and the inside pipe wall of cooling water outlet is 3-5cm, and wherein, the diameter of steam inlet is 1-3cm.
Described outlet is made up of entrance of cooling water and vapour outlet, and wherein vapour outlet is enclosed within entrance of cooling water.
Distance between the pipe outer wall of described vapour outlet and the inside pipe wall of entrance of cooling water is 3-5cm, and wherein, the diameter of vapour outlet is 2-5cm.
Described cooling tower has 20, and label is cooling tower a respectively, cooling tower b, cooling tower c, cooling tower d, cooling tower e, cooling tower f, cooling tower g, cooling tower h, cooling tower i, cooling tower j, cooling tower k, cooling tower l, cooling tower m, cooling tower n, cooling tower o, cooling tower p, cooling tower q, cooling tower r, cooling tower s, cooling tower t; Wherein the left cooling tower of cooling tower a is connected with cooling water outlet, and inner sleeve vapour stream siphunculus is connected with steam inlet, after cooling water outlet is connected with water pipe, coil in whole refrigerating unit according to flow direction with the vapour stream siphunculus of inner sleeve, the right cooling tower of cooling tower a is connected with the left cooling tower of cooling tower b; The right cooling tower of cooling tower b is connected with the left cooling tower of cooling tower f; The right cooling tower of cooling tower f is connected with the left cooling tower of cooling tower g; The right cooling tower of cooling tower g is connected with the right cooling tower of cooling tower h; The left cooling tower of cooling tower h is connected with the right cooling tower of cooling tower c; The left cooling tower of cooling tower c is connected with the left cooling tower of cooling tower d; The right cooling tower of cooling tower d is connected with the left cooling tower of cooling tower e; The right cooling tower of cooling tower e is connected with the left cooling tower of cooling tower i; The right cooling tower of cooling tower i is connected with the left cooling tower of cooling tower j; The right cooling tower of cooling tower j is connected with the left cooling tower of cooling tower o; The right cooling tower of cooling tower o is connected with the left cooling tower of cooling tower n; The right cooling tower of cooling tower n is connected with the left cooling tower of cooling tower m; The right cooling tower of cooling tower m is connected with the left cooling tower of cooling tower l; The right cooling tower of cooling tower l is connected with the left cooling tower of cooling tower k; The right cooling tower of cooling tower k is connected with the left cooling tower of cooling tower p; The right cooling tower of cooling tower p is connected with the left cooling tower of cooling tower q; The right cooling tower of cooling tower q is connected with the left cooling tower of cooling tower r; The right cooling tower of cooling tower r is connected with the left cooling tower of cooling tower s; The right cooling tower of cooling tower s is connected with the left cooling tower of cooling tower t; The right cooling tower of cooling tower t is connected with entrance of cooling water and vapour outlet.
What described cooling water outlet adopted is, and water pipe prepared by cast iron inserts in cooling tower coils; Described entrance of cooling water extends out after coiling in the water pipe insertion cooling tower adopting cast iron to prepare.
What described steam inlet adopted is coil in the pipe insertion cooling tower of ceramic preparation; Described vapour outlet adopts the pipe of ceramic preparation to insert in cooling tower to extend out after coiling.
Described pottery, its raw material comprises alumina particle and intersperses among the MgSi in alumina particle
2o
5be particle, wherein MgSi
2o
5be that after grinding to form 120-340 object powder after particle is mixed by aluminium, magnesium oxide, phosphogypsum, germanium oxide, silicon-dioxide, roasting is prepared from.
Above-mentioned maturing temperature is 1500-3000 DEG C.
Above-mentioned pottery, its material composition take parts by weight as alumina particle 50-80 part, MgSi
2o
5be particle be 13-77 part.
Above-mentioned MgSi
2o
5be the raw material in particle, its proportioning is according to any than mixing, and in the process of mixing, first employing stirring speed is after 100-400r/min stir process 20-30min, be placed on again in processor for ultrasonic wave, adopt frequency to be 30-50Hz process 40-90min, then carry out calcination process.
Above-mentioned roasting time is 1-3h.
Compared with prior art, technique effect of the present utility model is embodied in:
By improving the structure of refrigerating unit, make device by casing, be arranged on the cooling tower on casing, be arranged on the import on body side and be arranged on and form with the outlet arranged on the diagonally opposing corner of import opposite flank, and then make mercury vapour can realize water cycle cooling, and then make the duration of contact of water and steam longer, heat exchange degree is darker, and by the appropriate design to device, and then make the inner sheathed vapour stream siphunculus of water-cooled tube, and then mercury vapour to be leaked in environment and to pollute the probability of corrosion cooling tower outer wall lower, and then reduce the emission rate of mercury vapour, reduce environmental pollution rate, improve the cooling performance of mercuryvapour.
Limit especially by the distance between the inwall of the water pipe in device and the outer wall of vapour stream siphunculus, and limit in conjunction with to the size of import and the size of outlet, and then the time making the water coolant in device and mercury vapour carry out heat exchange is extended, and then the cooling performance that improve steam, again in conjunction with the inlet size of vapour stream siphunculus and the setting of outlet size, and then make steam setting aside some time in pipe longer, and water pipe and vapour stream siphunculus are repeatedly bent coiling, and then make steam and the water heat exchanger time in pipeline longer, and then improve cooling performance.
The mode combined again the bottom of the cooling tower on refrigerating unit is communicated with designs, and then makes the flushing time of water and steam in pipe, and coiling number of times is extended and increases, and then mercury vapour is effectively cooled.
Again by the setting of said structure, and then make refrigerating unit outer wall adopt cast iron preparation, vapour stream siphunculus adopts ceramic preparation, enhances the intensity of the outside of refrigerating unit, improves the heat transfer rate of water and steam, and then reduce energy consumption; And cast iron preparation is adopted in outside, and then make outside that multiple radiator element can be set, and then improve heat radiation, reduce the consumption of water coolant; Combine again and the raw material of pottery is chosen, and the process to raw material, make the stupalith prepared can meet mercury vapour and water carries out a large amount of heat exchanges, and then improve efficiency and the speed of exchanging heat, reduce cooling water amount, improve cooling performance.
Simultaneously, the utility model combines choosing ceramic raw material, and the processing mode to ceramic raw material, the intensity of the pottery prepared, plasticity-and heat transfer coefficient are improved all largely, and then ensure that steam inside circulation duct can carry out good heat exchange process with water coolant; And, adopt pottery and stupalith chosen and processes, and then make the corrosion resistance of the pottery prepared stronger, and then reduce cost prepared by device, also reduce the maintenance cost of follow up device, extend the work-ing life that mercury vapour adopts the device of water cycle cooling, reduce mercury vapour cooling cost.
Accompanying drawing explanation
Fig. 1 is the structural representation of water cycle of the present utility model cooling mercury vapour device.
Fig. 2 is the elevational schematic view after the bottom half of water cycle of the present utility model cooling mercury vapour device is cut open.
1-right cooling tower 2-left cooling tower 3-cooling tower 4-entrance of cooling water 5-vapour outlet 6-casing 7-cooling water outlet 8-steam inlet 9-flow direction 10-leakage pipe.
Embodiment
Below in conjunction with accompanying drawing and concrete embodiment, further restriction is done to the technical solution of the utility model, but claimed scope is not only confined to done description.
Water cycle cooling mercury vapour device of the present utility model is provided with leakage pipe at the left cooling tower 2 of each cooling tower and the knee, bottom of right cooling tower 1, and leakage pipe is communicated with vapour stream siphunculus, seals with water pipe.And be provided with in the bottom of leakage pipe and connect mercury tank.
Embodiment 1
As shown in Figure 1 and Figure 2, one water cycle cooling mercury vapour device, by casing 6, is arranged on the cooling tower 3 on casing 6, is arranged on the import on casing 6 side and is arranged on to form with the outlet arranged on the diagonally opposing corner of import opposite flank.Described cooling tower 3 has 20, and label is cooling tower a respectively, cooling tower b, cooling tower c, cooling tower d, cooling tower e, cooling tower f, cooling tower g, cooling tower h, cooling tower i, cooling tower j, cooling tower k, cooling tower l, cooling tower m, cooling tower n, cooling tower o, cooling tower p, cooling tower q, cooling tower r, cooling tower s, cooling tower t; Wherein the left cooling tower 2 of cooling tower a is connected with cooling water outlet 7, and inner sleeve vapour stream siphunculus is connected with steam inlet 8, after cooling water outlet 7 is connected with water pipe, coil in whole refrigerating unit according to flow direction 9 with the vapour stream siphunculus of inner sleeve, the right cooling tower 1 of cooling tower a is connected with the left cooling tower 2 of cooling tower b; The right cooling tower 1 of cooling tower b is connected with the left cooling tower 2 of cooling tower f; The right cooling tower 1 of cooling tower f is connected with the left cooling tower 2 of cooling tower g; The right cooling tower 1 of cooling tower g is connected with the right cooling tower 1 of cooling tower h; The left cooling tower 2 of cooling tower h is connected with the right cooling tower 1 of cooling tower c; The left cooling tower 2 of cooling tower c is connected with the left cooling tower 2 of cooling tower d; The right cooling tower 1 of cooling tower d is connected with the left cooling tower 2 of cooling tower e; The right cooling tower 1 of cooling tower e is connected with the left cooling tower 2 of cooling tower i; The right cooling tower 1 of cooling tower i is connected with the left cooling tower 2 of cooling tower j; The right cooling tower 1 of cooling tower j is connected with the left cooling tower 2 of cooling tower o; The right cooling tower 1 of cooling tower o is connected with the left cooling tower 2 of cooling tower n; The right cooling tower 1 of cooling tower n is connected with the left cooling tower 2 of cooling tower m; The right cooling tower 1 of cooling tower m is connected with the left cooling tower 2 of cooling tower l; The right cooling tower 1 of cooling tower l is connected with the left cooling tower 2 of cooling tower k; The right cooling tower 1 of cooling tower k is connected with the left cooling tower 2 of cooling tower p; The right cooling tower 1 of cooling tower p is connected with the left cooling tower 2 of cooling tower q; The right cooling tower 1 of cooling tower q is connected with the left cooling tower 2 of cooling tower r; The right cooling tower 1 of cooling tower r is connected with the left cooling tower 2 of cooling tower s; The right cooling tower 1 of cooling tower s is connected with the left cooling tower 2 of cooling tower t; The right cooling tower 1 of cooling tower t is connected with entrance of cooling water 4 and vapour outlet 5.
Embodiment 2
As shown in Figure 1, one water cycle cooling mercury vapour device, by casing 6, is arranged on the cooling tower 3 on casing 6, is arranged on the import on casing 6 side and is arranged on to form with the outlet arranged on the diagonally opposing corner of import opposite flank.Described cooling tower is made up of left cooling tower 2 and right cooling tower 1.Described import is made up of cooling water outlet 7 and steam inlet 8, and wherein, steam inlet 8 is enclosed within cooling water outlet 7.Described outlet is made up of entrance of cooling water 4 and vapour outlet 5, and wherein vapour outlet is enclosed within entrance of cooling water 4.
Embodiment 3
As shown in Fig. 1, Fig. 2, on the basis of embodiment 1, a kind of with water cycle cooling mercury vapour device, described cooling tower is made up of left cooling tower 2 and right cooling tower 1.Described import is made up of cooling water outlet 7 and steam inlet 8, and wherein, steam inlet 8 is enclosed within cooling water outlet 7.Described outlet is made up of entrance of cooling water 4 and vapour outlet 5, and wherein vapour outlet is enclosed within entrance of cooling water 4.
Embodiment 4
As shown in Figure 1 and Figure 2, at the based uplink of embodiment 3, the distance between the pipe outer wall of described steam inlet 8 and the inside pipe wall of cooling water outlet 7 is 4cm, and wherein, the diameter of steam inlet 8 is 2cm.Distance between the pipe outer wall of described vapour outlet 5 and the inside pipe wall of entrance of cooling water 4 is 4cm, and wherein, the diameter of vapour outlet 5 is 3cm.
Embodiment 5
As shown in Figure 1 and Figure 2, at the based uplink of embodiment 2, the distance between the pipe outer wall of described steam inlet 8 and the inside pipe wall of cooling water outlet 7 is 3cm, and wherein, the diameter of steam inlet 8 is 1cm.Distance between the pipe outer wall of described vapour outlet 5 and the inside pipe wall of entrance of cooling water 4 is 3cm, and wherein, the diameter of vapour outlet 5 is 2cm.
Embodiment 6
As shown in Figure 1 and Figure 2, at the based uplink of embodiment 1, the distance between the pipe outer wall of described steam inlet 8 and the inside pipe wall of cooling water outlet 7 is 5cm, and wherein, the diameter of steam inlet 8 is 3cm.Distance between the pipe outer wall of described vapour outlet 5 and the inside pipe wall of entrance of cooling water 4 is 5cm, and wherein, the diameter of vapour outlet 5 is 5cm.
Embodiment 7
As shown in Figure 1 and Figure 2, on the basis of embodiment 4, what described cooling water outlet 7 adopted is, and water pipe prepared by cast iron inserts in cooling tower 3 coils; Described entrance of cooling water 4 extends out after coiling in the water pipe insertion cooling tower 3 adopting cast iron to prepare.What described steam inlet 8 adopted is coil in the pipe insertion cooling tower 3 of ceramic preparation; Described vapour outlet 5 adopts the pipe of ceramic preparation to insert in cooling tower 3 to extend out after coiling.
Embodiment 8
As shown in Figure 1 and Figure 2, on the basis of embodiment 7, described pottery, its raw material comprises alumina particle and intersperses among the MgSi in alumina particle
2o
5be particle, wherein MgSi
2o
5be that after grinding to form 120 object powder after particle is mixed by aluminium, magnesium oxide, phosphogypsum, germanium oxide, silicon-dioxide, roasting is prepared from.Above-mentioned maturing temperature is 1500 DEG C.Above-mentioned pottery, its material composition is alumina particle 50kg, MgSi by weight
2o
5be particle be 13kg.Above-mentioned MgSi
2o
5be the raw material in particle, its proportioning is according to any than mixing, and in the process of mixing, first employing stirring speed is after 100r/min stir process 20min, be placed on again in processor for ultrasonic wave, adopt frequency to be 30Hz process 40min, then carry out calcination process.Above-mentioned roasting time is 1h.
Embodiment 9
As shown in Figure 1 and Figure 2, on the basis of embodiment 7, described pottery, its raw material comprises alumina particle and intersperses among the MgSi in alumina particle
2o
5be particle, wherein MgSi
2o
5be that after grinding to form 340 object powder after particle is mixed by aluminium, magnesium oxide, phosphogypsum, germanium oxide, silicon-dioxide, roasting is prepared from.Above-mentioned maturing temperature is 3000 DEG C.Above-mentioned pottery, its material composition is alumina particle 80kg, MgSi by weight
2o
5be particle be 77kg.Above-mentioned MgSi
2o
5be the raw material in particle, its proportioning is according to any than mixing, and in the process of mixing, first employing stirring speed is after 400r/min stir process 30min, be placed on again in processor for ultrasonic wave, adopt frequency to be 50Hz process 90min, then carry out calcination process.Above-mentioned roasting time is 3h.
Embodiment 10
As shown in Figure 1 and Figure 2, on the basis of embodiment 7, described pottery, its raw material comprises alumina particle and intersperses among the MgSi in alumina particle
2o
5be particle, wherein MgSi
2o
5be that after grinding to form 300 object powder after particle is mixed by aluminium, magnesium oxide, phosphogypsum, germanium oxide, silicon-dioxide, roasting is prepared from.Above-mentioned maturing temperature is 2000 DEG C.Above-mentioned pottery, its material composition is alumina particle 75kg, MgSi by weight
2o
5be particle be 56kg.Above-mentioned MgSi
2o
5be the raw material in particle, its proportioning is according to any than mixing, and in the process of mixing, first employing stirring speed is after 300r/min stir process 25min, be placed on again in processor for ultrasonic wave, adopt frequency to be 40Hz process 50min, then carry out calcination process.Above-mentioned roasting time is 2h.
Claims (9)
1. one kind cools mercury vapour device by water cycle, it is characterized in that, by casing (6), be arranged on the cooling tower (3) on casing (6), be arranged on the import on casing (6) side and be arranged on and form with the outlet arranged on the diagonally opposing corner of import opposite flank.
2., as claimed in claim 1 with water cycle cooling mercury vapour device, it is characterized in that, described cooling tower is made up of left cooling tower (2) and right cooling tower (1).
3. as claimed in claim 1 with water cycle cooling mercury vapour device, it is characterized in that, described import is made up of cooling water outlet (7) and steam inlet (8), and wherein, steam inlet (8) is enclosed within cooling water outlet (7).
4. as claimed in claim 3 with water cycle cooling mercury vapour device, it is characterized in that, distance between the pipe outer wall of described steam inlet (8) and the inside pipe wall of cooling water outlet (7) is 3-5cm, and wherein, the diameter of steam inlet (8) is 1-3cm.
5., as claimed in claim 1 with water cycle cooling mercury vapour device, it is characterized in that, described outlet is made up of entrance of cooling water (4) and vapour outlet (5), and wherein vapour outlet is enclosed within entrance of cooling water (4).
6. as claimed in claim 5 with water cycle cooling mercury vapour device, it is characterized in that, distance between the pipe outer wall of described vapour outlet (5) and the inside pipe wall of entrance of cooling water (4) is 3-5cm, and wherein, the diameter of vapour outlet (5) is 2-5cm.
7. as described in any one of claim 1-6 with water cycle cooling mercury vapour device, it is characterized in that, described cooling tower (3) has 20, and label is cooling tower a respectively, cooling tower b, cooling tower c, cooling tower d, cooling tower e, cooling tower f, cooling tower g, cooling tower h, cooling tower i, cooling tower j, cooling tower k, cooling tower l, cooling tower m, cooling tower n, cooling tower o, cooling tower p, cooling tower q, cooling tower r, cooling tower s, cooling tower t; Wherein the left cooling tower (2) of cooling tower a is connected with cooling water outlet (7), and inner sleeve vapour stream siphunculus is connected with steam inlet (8), after cooling water outlet (7) is connected with water pipe, coil in whole refrigerating unit according to flow direction (9) with the vapour stream siphunculus of inner sleeve, the right cooling tower (1) of cooling tower a is connected with the left cooling tower (2) of cooling tower b; The right cooling tower (1) of cooling tower b is connected with the left cooling tower (2) of cooling tower f; The right cooling tower (1) of cooling tower f is connected with the left cooling tower (2) of cooling tower g; The right cooling tower (1) of cooling tower g is connected with the right cooling tower (1) of cooling tower h; The left cooling tower (2) of cooling tower h is connected with the right cooling tower (1) of cooling tower c; The left cooling tower (2) of cooling tower c is connected with the left cooling tower (2) of cooling tower d; The right cooling tower (1) of cooling tower d is connected with the left cooling tower (2) of cooling tower e; The right cooling tower (1) of cooling tower e is connected with the left cooling tower (2) of cooling tower i; The right cooling tower (1) of cooling tower i is connected with the left cooling tower (2) of cooling tower j; The right cooling tower (1) of cooling tower j is connected with the left cooling tower (2) of cooling tower o; The right cooling tower (1) of cooling tower o is connected with the left cooling tower (2) of cooling tower n; The right cooling tower (1) of cooling tower n is connected with the left cooling tower (2) of cooling tower m; The right cooling tower (1) of cooling tower m is connected with the left cooling tower (2) of cooling tower l; The right cooling tower (1) of cooling tower l is connected with the left cooling tower (2) of cooling tower k; The right cooling tower (1) of cooling tower k is connected with the left cooling tower (2) of cooling tower p; The right cooling tower (1) of cooling tower p is connected with the left cooling tower (2) of cooling tower q; The right cooling tower (1) of cooling tower q is connected with the left cooling tower (2) of cooling tower r; The right cooling tower (1) of cooling tower r is connected with the left cooling tower (2) of cooling tower s; The right cooling tower (1) of cooling tower s is connected with the left cooling tower (2) of cooling tower t; The right cooling tower (1) of cooling tower t is connected with entrance of cooling water (4) and vapour outlet (5).
8. as claimed in claim 3 with water cycle cooling mercury vapour device, it is characterized in that, what described cooling water outlet (7) adopted is, and water pipe prepared by cast iron inserts in cooling tower (3) coils; Described entrance of cooling water (4) extends out after the water pipe adopting cast iron to prepare inserts the middle coiling of cooling tower (3).
9. as claimed in claim 3 with water cycle cooling mercury vapour device, it is characterized in that, what described steam inlet (8) adopted is coil in pipe insertion cooling tower (3) of ceramic preparation; Described vapour outlet (5) adopts the pipe of ceramic preparation to insert in cooling tower (3) to extend out after coiling.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520721481.5U CN204939590U (en) | 2015-09-17 | 2015-09-17 | A kind of with water cycle cooling mercury vapour device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520721481.5U CN204939590U (en) | 2015-09-17 | 2015-09-17 | A kind of with water cycle cooling mercury vapour device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204939590U true CN204939590U (en) | 2016-01-06 |
Family
ID=55007033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520721481.5U Expired - Fee Related CN204939590U (en) | 2015-09-17 | 2015-09-17 | A kind of with water cycle cooling mercury vapour device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204939590U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105132716A (en) * | 2015-09-17 | 2015-12-09 | 贵州蓝天固废处置有限公司 | Device for cooling mercury vapor through water circulation |
-
2015
- 2015-09-17 CN CN201520721481.5U patent/CN204939590U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105132716A (en) * | 2015-09-17 | 2015-12-09 | 贵州蓝天固废处置有限公司 | Device for cooling mercury vapor through water circulation |
CN105132716B (en) * | 2015-09-17 | 2017-11-14 | 贵州蓝天固废处置有限公司 | It is a kind of to cool down mercury vapour device with water circulation |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106591727A (en) | Corrosion-resistant and high-temperature-resistant shell for oil-immersed transformer | |
CN204939590U (en) | A kind of with water cycle cooling mercury vapour device | |
CN105132716A (en) | Device for cooling mercury vapor through water circulation | |
CN104197758A (en) | Superconductive heat pipe and heat transfer medium thereof | |
CN202432587U (en) | Heat supply unit using cement kiln waste heat | |
CN104457287A (en) | Double-cooling slag cooler of metallic magnesium reducing slag waste heat utilization system | |
CN203425752U (en) | Mixer device with heating and cooling functions | |
CN207966672U (en) | A kind of dry-type transformer with rapid cooling function | |
CN103331446B (en) | Low-temperature hot air circulation heat treatment furnace for magnetic core and application method of heat treatment furnace | |
CN202954072U (en) | Special cooling device for closed internal circulation gas shield copper wire vacuum annealing furnace | |
CN206169214U (en) | Cooling device is used in magnetite production | |
CN202350292U (en) | Straight energy-saving heating water boiler | |
CN204359175U (en) | A kind of warm sludge cooling heat exchanger | |
CN205590750U (en) | A quenching groove that is used for in turn thermal treatment ball of water -cooling air cooling | |
CN204854373U (en) | Cotton smelting pot waste heat reutilization system of glass | |
CN204589275U (en) | A kind of heating of high-purity rare-earth feed liquid or refrigerating unit | |
CN206692701U (en) | A kind of energy-saving electromagnetic stirring type aluminium holding furnace | |
CN110267489A (en) | A kind of de- alloy reaction prepares the device and method of porous microchannel | |
CN202315860U (en) | Reaction kettle capable of heating and cooling fast | |
CN206874458U (en) | A kind of waste heat recovery utilizing equipment | |
CN201569285U (en) | Smelting sheet casting furnace | |
CN204039292U (en) | A kind of efficient chloridizing unit | |
CN205392202U (en) | Novel salt water pond | |
CN203203253U (en) | Water tank with liner outside-coiling condenser pipe device inside metal sleeve | |
CN204063992U (en) | A kind of kiln waste heat utilization system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160106 Termination date: 20180917 |