CN209475918U - The condensation water recovery and use system of high temperature cigarette vapour - Google Patents

The condensation water recovery and use system of high temperature cigarette vapour Download PDF

Info

Publication number
CN209475918U
CN209475918U CN201822169261.2U CN201822169261U CN209475918U CN 209475918 U CN209475918 U CN 209475918U CN 201822169261 U CN201822169261 U CN 201822169261U CN 209475918 U CN209475918 U CN 209475918U
Authority
CN
China
Prior art keywords
pipe
water
high temperature
condensation
storage tank
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.)
Active
Application number
CN201822169261.2U
Other languages
Chinese (zh)
Inventor
杨鲁旭
徐大立
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu Greenland Heat Transfer Technology Co Ltd
Original Assignee
Jiangsu Greenland Heat Transfer Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jiangsu Greenland Heat Transfer Technology Co Ltd filed Critical Jiangsu Greenland Heat Transfer Technology Co Ltd
Priority to CN201822169261.2U priority Critical patent/CN209475918U/en
Application granted granted Critical
Publication of CN209475918U publication Critical patent/CN209475918U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses the processing technology fields of high temperature cigarette vapour, it is intended to provide a kind of condensation water recovery and use system of high temperature cigarette vapour, its key points of the technical solution are that including that evaporation is cold, it evaporates in cold and is from top to bottom successively arranged gilled radiator, spray tube and condensation tubulation, cold top is evaporated equipped with cooling fan, bottom is equipped with water storage tank, water storage tank is communicated with water-supply-pipe, condensation tubulation is communicated with steam absorbing tube, gilled radiator is communicated with escape pipe, the first isocon is parallel on steam absorbing tube, first isocon is connected to gilled radiator, the second isocon is parallel on escape pipe, second isocon is connected to condensation tubulation, gilled radiator is communicated with outlet pipe, condensation tubulation is communicated with branched pipe, branched pipe is connected to outlet pipe.The utility model is carried out jointly using air-cooled and water cooling two ways, and the loss of cost can also be reduced while cooling a large amount of condensed waters out, has and uses meaning.

Description

The condensation water recovery and use system of high temperature cigarette vapour
Technical field
The utility model relates to the processing technology field of high temperature cigarette vapour, in particular to a kind of condensing hot air furnace of high temperature cigarette vapour Utilize system.
Background technique
High temperature cigarette vapour refers in the technical fields such as intermetallic composite coating and grain-drying, is arranged by heating equipment or drying equipment Cigarette vapour out.In the quenching technical of intermetallic composite coating, need regularly to carry out water supply during part is processed, with This makes the part of processing have more excellent mechanical property, thus in cigarette vapour would generally containing it is more due to by thermal evaporation and The steam of generation.During grain-drying, the moisture in cereal is heated and overflows cereal, so that drying equipment is arranged Equally there is more moisture in smoke vapour.
Currently, the Chinese patent that notification number is CN103697730B discloses a kind of high temperature cigarette vapour flash cooler, it is wrapped Include shell, air cooling pipe, air cooling pipe is mounted in shell, it is characterized in that on the two sides side plate of the positive apparent direction of shell vertical welding every Plate forms S-shaped channel in shell;Partition is porous plate, and hole count is identical as the quantity of air cooling pipe, and air cooling pipe passes through on partition Hole passes through partition, is welded on partition;Air cooling pipe is the not closed hollow steel pipe in both ends, and the cooling medium in air cooling pipe is empty Gas, air generate flowing, bottom in and top out using stack effect in air cooling pipe;High-temperature flue gas upper entering and lower leaving does S-shaped in shell Flowing, while heat exchange is streamed outside air cooling pipe, catch basin is welded on the top plate top of shell;Header tank is installed in the lower part of the housing, Spray head is installed at an upper portion thereof;Header tank is connect by water circulating pump and water supplying pipe with spray head.
During the work time, high temperature cigarette vapour enters this high temperature cigarette vapour flash cooler at the top of cooler, bottom discharge, Heat exchange is carried out by the cold water in the spray head and air cooling pipe of top, to realize the cooling to cigarette vapour.Due in high temperature cigarette vapour Moisture is usually contained, during cooling cigarette vapour, the moisture in cigarette vapour can condense to form water flow.And this high temperature cigarette vapour is quick In cooler, water flow is consistent with the migration route of gas, be discharge shell outside, can not carry out moisture collection and again benefit With wasting vast resources.
Utility model content
The purpose of the utility model is to provide a kind of condensation water recovery and use systems of high temperature cigarette vapour, have and damage in low cost In the case where consumption, the advantages of recycling and reusing condensed water.
The above-mentioned technical purpose of the utility model has the technical scheme that
A kind of condensation water recovery and use system of high temperature cigarette vapour, including evaporation are cold, in the evaporation is cold from top to bottom successively Equipped with gilled radiator, spray tube and condensation tubulation, the cold top of the evaporation is equipped with cooling fan, the cold bottom of the evaporation Portion is equipped with water storage tank, and the water storage tank is communicated with water-supply-pipe, and the water-supply-pipe is connected to spray tube, is connected on the water-supply-pipe First suction pump, one end of the condensation tubulation are communicated with steam absorbing tube, and the gilled radiator connects away from one end of steam absorbing tube It is connected with escape pipe, the first isocon is parallel on the steam absorbing tube, it is separate that first isocon is connected to gilled radiator One end of escape pipe, is parallel with the second isocon on the escape pipe, and second isocon is connected to condensation tubulation away from inhaling One end of steam pipe, one end of the gilled radiator towards escape pipe are communicated with outlet pipe, and the outlet pipe is connected to water storage One end of slot, the condensation tubulation towards the second isocon is communicated with branched pipe, and the branched pipe is connected to outlet pipe.
By using above-mentioned technical proposal, during the work time, towards steam absorbing tube in pour high temperature cigarette vapour, high temperature cigarette vapour according to It is secondary to enter in gilled radiator and condensation tubulation.High temperature cigarette vapour in condensation tubulation is carried out cold using the water flow in spray tube But, since principle of conservation of energy, condensation tubulation cooling are formed by water, the evaporation capacity for spraying interior water with spray tube is roughly equal, The two mutually balances each other, can not surplus go out more condensed waters and recycled.High temperature cigarette vapour warp in the gilled radiator of setting Supercooling blower is cooled down, be not necessarily to waste water resource, therefore the condensed water in gilled radiator can by outlet pipe into Enter in water storage tank, so that the evaporation cold energy in the utility model, which reaches surplus, goes out extra condensed water for other workshop sections.? In high temperature cigarette vapour treatment process, although a large amount of cooling water can be cooled down out using pure air-cooled form, cooling wind is driven Machine is needed using a large amount of electric power, while the later period is also required to biggish expense to the maintenance of cooling blower, does not utilize very much cost It saves, in the utility model, is carried out jointly using air-cooled and water cooling two ways, it can also while cooling a large amount of condensed waters out The loss of cost is reduced, has and uses meaning.
Further, the pipe shaft that the outlet pipe is located at below gilled radiator is bent with the first U-shaped curved, water outlet It is U-shaped curved that the pipe shaft that pipe is located at below branched pipe is bent with second.
By using above-mentioned technical proposal, when condensed water in gilled radiator and condensation tubulation by flowing out, can be attached to few The gas of amount.For condensed water U-shaped curved and when second is U-shaped curved by first, condensed water can pass through an elder generation upward mistake again downwards Journey, and according to the natural law it can be concluded that, condensed water is downward, and gas moves upwards, condensed water by first downwards it is upward again In the process, due to the influence of gravity, first is U-shaped curved and the second U-shaped curved bending place can make the speed of condensed water slow down, condensation Water is thus of short duration to be gathered in first U-shaped curved and the second U-shaped curved bending place, and gas can not be circulated by the bending place at this time, only It can be back in gilled radiator and condensation tubulation, be discharged by escape pipe.
Further, sewer pipe is communicated with below the water storage tank, the sewer pipe is equipped with the second suction pump, described Pipe shaft of the sewer pipe between the second suction pump and water storage tank is equipped with opening and closing ball valve.
By using above-mentioned technical proposal, the water flow in water storage tank after carrying out multiple circulating cooling to condensation tubulation, Impurity will certainly wherein be contained, in order to which impurity blocks spray tube, be provided with sewer pipe.Sewer pipe passes through the suction of the second suction pump Power, so that the impurity and raffinate in water storage tank are extracted by sewer pipe.
Further, first isocon is equipped with flow control valve.
By using above-mentioned technical proposal, the size that flow control valve is capable of circulation bore to the first isocon is adjusted Section, can be adjusted with this according to required condensed water.When needing more condensed water, flow control valve is adjusted, so that The circulation bore of first isocon increases, and more cigarette vapour can enter in gilled radiator, reduce high-temperature flue gas enter it is cold The amount of solidifying tubulation.When due to water cooling, the water flow that the cigarette vapour is cooled into (conservation of energy consistent with the water flow sprayed in spray tube Law), therefore generally water will not generate variation.And when carrying out air-cooled, it is only necessary to consume air quantity, the wave without water flow Take, therefore generally can water be increased.
Further, gas-liquid partition is equipped between the gilled radiator and spray tube, the gas-liquid partition is by several Steel screen layer stacks gradually.
By using above-mentioned technical proposal, the water flow that spray tube sprays is when cooling down condensation tubulation, water flow due to by Heat can generate Evaporation Phenomenon.Gas-liquid partition is made of steel screen layer, resistance of the water mist of evaporation when rising, by gas-liquid partition Every the water flow in water mist can be trapped in steel screen layer by gas-liquid partition, reduce the amount that water mist enters air-cooled region.
Further, fluid reservoir is communicated on the outlet pipe, the fluid reservoir is equipped with liquidometer, the outlet pipe position Pipe shaft between fluid reservoir and water storage tank is equipped with control ball valve.
By using above-mentioned technical proposal, fluid reservoir is for storing extra liquid, to improve the storage of the utility model Outlet capacity.
Further, constant pressure supply water tank, institute are communicated on pipe shaft of the outlet pipe between fluid reservoir and water storage tank Pipe shaft of the outlet pipe between fluid reservoir and constant pressure supply water tank is stated equipped with third suction pump.
By using above-mentioned technical proposal, when water flow in fluid reservoir by flowing out, successively mended by third suction pump and level pressure Water pot, third suction pump are used to improve the speed of water flow, and constant pressure supply water tank is used to stablize the pressure of water body, so that water flow has There is constant pressure to flow out out of constant pressure supply water tank, ensure that speed when water flow is flowed out out of constant pressure supply water tank.
Further, the outlet pipe is equipped with water treatment facilities close to the pipe shaft of water storage tank, and the outlet pipe is located at water Spare pipe is parallel on pipe shaft between processing equipment and water storage tank, the spare pipe is equipped with the first ball valve, the outlet pipe Pipe shaft close to water storage tank is equipped with the second ball valve.
By using above-mentioned technical proposal, water treatment facilities can carry out purified treatment to condensed water, to reduce condensation Impurity content in water.The setting of spare pipe is for connecting other using workshop section, to improve condensed water in the utility model Use scope.
Further, pipe shaft of first isocon between flow control valve and steam absorbing tube is curved equipped with transition, The curved transition is vertically arranged semicircle shape.
By using above-mentioned technical proposal, due to high-temperature flue gas temperature with higher, the excessively high meeting of temperature is so that first point Flow tube generates the effect expanded with heat and contract with cold, and the curved setting of transition is so that the first isocon when thermal expansion and cold contraction effect occurs, generates change Shape, to reduce a possibility that the first isocon produces fracture.
In conclusion the utility model has the following beneficial effects: the utility model is using air-cooled and water cooling two ways Common to carry out, the air-cooled condensed water for being used to form surplus, water cooling plays the role of mainly cooling down high temperature cigarette vapour, compared to air-cooled, Water cooling is only the heat exchange between substance and substance, therefore more energy saving, to reach in cooling a large amount of condensed waters out While the advantages of can also reducing cost loss, have in the processing metal field of high temperature cigarette vapour and use meaning.
Detailed description of the invention
Fig. 1 is the structural schematic diagram for embodying the utility model.
In figure, 1, evaporation it is cold;11, gilled radiator;12, spray tube;13, condensation tubulation;131, branched pipe;14, cold But fan;15, water storage tank;2, water-supply-pipe;21, the first suction pump;3, steam absorbing tube;31, the first isocon;311, flow is adjusted Valve;312, transition is curved;4, escape pipe;41, the second isocon;5, outlet pipe;51, first is U-shaped curved;52, second is U-shaped curved;53, it stores up Flow container;531 liquidometers;54, ball valve is controlled;55, constant pressure supply water tank;56, third suction pump;57, spare pipe;571, the first ball Valve;58, the second ball valve;6, sewer pipe;61, the second suction pump;62, ball valve is opened and closed;7, gas-liquid partition;8, water treatment facilities.
Specific embodiment
The utility model is described in further detail below in conjunction with attached drawing.
Embodiment: a kind of condensation water recovery and use system of high temperature cigarette vapour, referring to Fig.1, including evaporation cold 1, it evaporates in cold 1 It is from top to bottom successively arranged gilled radiator 11, spray tube 12 and condensation tubulation 13, the top of evaporation cold 1 is equipped with cooling fan 14, cooling fan 14 is set in qually spaced in the top of evaporation cold 1.Finned cooling fin is right against cooling fan 14.
Referring to Fig.1, the bottom of evaporation cold 1 is equipped with water storage tank 15, and water storage tank 15 is communicated with water-supply-pipe 2, and outlet pipe 5 is connected to Spray tube 12.The first suction pump 21 is communicated on water-supply-pipe 2, the first suction pump 21 increases the pressure in water-supply-pipe 2, makes Obtaining water-supply-pipe 2 can more effectively be delivered to the water in water storage tank 15 in spray tube 12.
Referring to Fig.1, one end of condensation tubulation 13 is communicated with steam absorbing tube 3, and gilled radiator 11 deviates from one end of steam absorbing tube 3 It is communicated with escape pipe 4, the first isocon 31 is parallel on steam absorbing tube 3, it is remote that the first isocon 31 is connected to gilled radiator 11 Separate out one end of tracheae 4.The second isocon 41 is parallel on escape pipe 4, the second isocon 41, which is connected to condensation tubulation 13, to deviate from One end of steam absorbing tube 3.One end of gilled radiator 11 towards escape pipe 4 is communicated with outlet pipe 5, and outlet pipe 5 is connected to water storage Slot 15.One end of condensation tubulation 13 towards the second isocon 41 is communicated with branched pipe 131, and branched pipe 131 is connected to outlet pipe 5. Branched pipe 131 and outlet pipe 5 cooperate jointly, so that the water flow in gilled radiator 11 and condensation tubulation 13 flow to water storage tank 15 It is interior.
Referring to Fig.1, in high temperature cigarette vapour treatment process, although can be cooled down out using pure air-cooled form a large amount of cooling Water, however drive cooling blower to need using a large amount of electric power, while the later period is also required to biggish expense to the maintenance of cooling blower With not utilizing very much the saving of cost.In the utility model, carried out jointly using air-cooled and water cooling two ways, it is big out in cooling The loss of cost can also be reduced while measuring condensed water, had and used meaning.
Referring to Fig.1, during the work time, towards high temperature cigarette vapour is poured in steam absorbing tube 3, high temperature cigarette vapour sequentially enters finned In radiator 11 and condensation tubulation 13.High temperature cigarette vapour in condensation tubulation 13 is cooled down using the water flow in spray tube 12, by In principle of conservation of energy, the cooling of condensation tubulation 13 is formed by water, and the evaporation capacity for spraying interior water with spray tube 12 is roughly equal, and two Person mutually balances each other, can not surplus go out more condensed waters and recycled.High temperature cigarette vapour warp in the gilled radiator 11 of setting Supercooling blower is cooled down, and is not necessarily to waste water resource, therefore the condensed water in gilled radiator 11 can pass through outlet pipe 5 Into in water storage tank 15 so that evaporation cold 1 in the utility model can surplus go out extra condensed water for other works Section.
Referring to Fig.1, the pipe shaft that outlet pipe 5 is located at 11 lower section of gilled radiator is bent with first U-shaped curved 51, outlet pipe 5 Pipe shaft positioned at 131 lower section of branched pipe is bent with second U-shaped curved 52.When condensed water is by gilled radiator 11 and condensation tubulation 13 When interior outflow, condensed water will certainly take a small amount of gas out of, when condensed water is at by first U-shaped curved 51 and second U-shaped curved 52, Since water is walked downwards, gas is upward, and at U-shaped region, water can temporarily be deposited in U-shaped bottom, to block the warp of gas U-shaped region is crossed, as condensed water constantly enters in outlet pipe 5, gas is squeezed and flows out outlet pipe 5.
Referring to Fig.1, it is communicated with sewer pipe 6 in the lower section of water storage tank 15, sewer pipe 6 is equipped with the second suction pump 61, waste liquid Pipe shaft of the pipe 6 between the second suction pump 61 and water storage tank 15 is equipped with opening and closing ball valve 62.Sewer pipe 6 can be stored up to being trapped in Residue in sink 15 is cleared up, and residue is sucked out using the suction of the second suction pump 61.
Referring to Fig.1, flow control valve 311 is equipped on the first isocon 31, flow control valve 311 can be to high temperature cigarette vapour The amount for entering gilled radiator 11 is adjusted, and when needing more condensed water, tunes up opening for flow control valve 311 Mouthful, so that more high temperature cigarette vapour enter in flow control valve 311, gilled radiator 11 is cooling by the way of air-cooled, nothing Water resource need to be evaporated, the amount of cooling water of condensed water is improved.
Referring to Fig.1, the water of spray tube 12 is sprayed onto condensation tubulation 13, and the heat of high temperature cigarette vapour makes in condensation tubulation 13 The water that spray tube 12 sprays generates evaporation, gilled radiator 11 is risen in order to reduce the steam of evaporation, in finned heat dissipation Gas-liquid partition 7 is equipped between device 11 and spray tube 12, gas-liquid partition 7 is stacked gradually by several steel screen layers.The steaming of evaporation When vapour is reached at gas-liquid partition, the liquid in steam rests on gas-liquid partition 7 by the interception of several steel screen layers, for a long time The water flow being trapped on steel screen layer afterwards is fallen in water storage tank 15, so that reducing steam touches gilled radiator 11 Amount, improves air-cooled cooling efficiency.
Referring to Fig.1, fluid reservoir 53 is communicated on outlet pipe 5, fluid reservoir 53 is equipped with liquidometer (not marking in figure), out Pipe shaft of the water pipe 5 between fluid reservoir 53 and water storage tank 15 is equipped with control ball valve 54.The condensed water flowed in outlet pipe 5 is first It is introduced into water storage tank 15, it is cold in outlet pipe 5 when the amount needed for the water in water storage tank 15 meets cooling condensation tubulation 13 Condensate, which enters in fluid reservoir 53, to be stored, and liquidometer is used to show the height of water level in fluid reservoir 53.Outlet pipe 5, which is located at, to be stored up Constant pressure supply water tank 55 is equipped between flow container 53 and water storage tank 15, outlet pipe 5 is communicated with constant pressure supply water tank 55.In fluid reservoir 53 and determine It presses and is equipped with third suction pump 56 between replenisher tank 55, third suction pump 56 is connected on the pipe shaft of outlet pipe 5.Constant pressure supply water tank 55 Interior to have stable pressure, when the water in fluid reservoir 53 is extracted out by the first suction pump 21, condensed water first passes around level pressure benefit In water pot 55, condensed water realizes pressurization in constant pressure supply water tank 55, to have bigger flow velocity to flow in outlet pipe 5.
Referring to Fig.1, outlet pipe 5 is equipped with water treatment facilities 8, water treatment facilities 8 and water storage close to the pipe shaft of water storage tank 15 It is parallel with spare pipe 57 on pipe shaft between slot 15, the first ball valve 571 is equipped on spare pipe 57, outlet pipe 5 is close to water storage tank 15 pipe shaft is equipped with the second ball valve 58.Water treatment facilities 8 can filter out the magazine in condensed water, cold to reach purification The effect of condensate.Spare pipe 57 with the pipeline of other workshop sections for being connected.
Referring to Fig.1, it is curved to be equipped with transition for pipe shaft of first isocon 31 between flow control valve 311 and steam absorbing tube 3 312, transition curved 312 is vertically arranged semicircle shape.For high temperature cigarette vapour when by the first isocon 31, high temperature can make pipeline Thermal expansion and cold contraction effect is generated, the transition of setting curved 312 can offset the expansion caused by high temperature cigarette vapour, reduce by first and shunt A possibility that pipe 31 produces fracture.
Specific implementation process:
1, high temperature cigarette vapour is entered in condensation tubulation 13 and gilled radiator 11 by steam inlet pipe, by adjusting flow control valve 311, adjustment high temperature cigarette vapour has respectively entered the amount in condensation tubulation 13 and gilled radiator 11;
2, start cooling blower and the first suction pump 21, cooling blower carries out the high temperature cigarette vapour in gilled radiator 11 Cooling, the water in water storage tank 15 is evacuated in spray tube 12 by the first suction pump 21, and the water that spray tube 12 sprays is to condensation tubulation 13 Interior water is cooled down, to achieve the purpose that cooling high temperature cigarette vapour;
3, the condensed water in condensation tubulation 13 and gilled radiator 11 is recycled to fluid reservoir 53 and water storage by outlet pipe 5 In slot 15, it is achieved in the recycling and reusing to condensed water.
This specific embodiment is only the explanation to the utility model, is not limitations of the present invention, ability Field technique personnel can according to need the modification that not creative contribution is made to the present embodiment after reading this specification, but As long as all by the protection of Patent Law in the scope of the claims of the utility model.

Claims (9)

1. a kind of condensation water recovery and use system of high temperature cigarette vapour, it is characterised in that: including evaporating cold (1), the evaporation cold (1) Inside from top to bottom it is successively arranged gilled radiator (11), spray tube (12) and condensation tubulation (13), the top for evaporating cold (1) Portion is equipped with cooling fan (14), and the bottom for evaporating cold (1) is equipped with water storage tank (15), and the water storage tank (15) is communicated with water delivery It manages (2), the water-supply-pipe (2) is connected to spray tube (12), is connected with the first suction pump (21) on the water-supply-pipe (2), described One end of condensation tubulation (13) is communicated with steam absorbing tube (3), and the gilled radiator (11) is connected to away from the one end of steam absorbing tube (3) Have escape pipe (4), be parallel with the first isocon (31) on the steam absorbing tube (3), first isocon (31) is connected to fin The one end of formula radiator (11) far from escape pipe (4), is parallel with the second isocon (41) on the escape pipe (4), described second Isocon (41) is connected to one end that condensation tubulation (13) deviate from steam absorbing tube (3), and the gilled radiator (11) is towards outlet One end of pipe (4) is communicated with outlet pipe (5), and the outlet pipe (5) is connected to water storage tank (15), condensation tubulation (13) direction One end of second isocon (41) is communicated with branched pipe (131), and the branched pipe (131) is connected to outlet pipe (5).
2. the condensation water recovery and use system of high temperature cigarette vapour according to claim 1, it is characterised in that: the outlet pipe (5) it is located at the pipe shaft below gilled radiator (11) and is bent with first U-shaped curved (51), the outlet pipe (5) is located at branched pipe (131) pipe shaft below is bent with second U-shaped curved (52).
3. the condensation water recovery and use system of high temperature cigarette vapour according to claim 1, it is characterised in that: the water storage tank (15) it is communicated with below sewer pipe (6), the sewer pipe (6) is equipped with the second suction pump (61), and the sewer pipe (6) is located at Pipe shaft between second suction pump (61) and water storage tank (15) is equipped with opening and closing ball valve (62).
4. the condensation water recovery and use system of high temperature cigarette vapour according to claim 1, it is characterised in that: described first shunts It manages (31) and is equipped with flow control valve (311).
5. the condensation water recovery and use system of high temperature cigarette vapour according to claim 1, it is characterised in that: described finned scattered Gas-liquid partition (7) are equipped between hot device (11) and spray tube (12), the gas-liquid partition (7) is stacked gradually by several steel screen layers It forms.
6. the condensation water recovery and use system of high temperature cigarette vapour according to claim 1, it is characterised in that: the outlet pipe (5) it is communicated on fluid reservoir (53), the fluid reservoir (53) is equipped with liquidometer, and the outlet pipe (5) is located at fluid reservoir (53) Pipe shaft between water storage tank (15) is equipped with control ball valve (54).
7. the condensation water recovery and use system of high temperature cigarette vapour according to claim 6, it is characterised in that: the outlet pipe (5) it is communicated with constant pressure supply water tank (55) on the pipe shaft between fluid reservoir (53) and water storage tank (15), outlet pipe (5) position Pipe shaft between fluid reservoir (53) and constant pressure supply water tank (55) is equipped with third suction pump (56).
8. the condensation water recovery and use system of high temperature cigarette vapour according to claim 1, it is characterised in that: the outlet pipe (5) pipe shaft close to water storage tank (15) is equipped with water treatment facilities (8), and the outlet pipe (5) is located at water treatment facilities and water storage It is parallel on pipe shaft between slot (15) spare pipe (57), the spare pipe is equipped with the first ball valve (571), the outlet pipe (5) pipe shaft close to water storage tank (15) is equipped with the second ball valve (58).
9. the condensation water recovery and use system of high temperature cigarette vapour according to claim 1, it is characterised in that: described first shunts Pipe (31) be located at the pipe shaft between flow control valve (311) and steam absorbing tube (3) be equipped with transition it is curved (312), the transition is curved It (312) is vertically arranged semicircle shape.
CN201822169261.2U 2018-12-21 2018-12-21 The condensation water recovery and use system of high temperature cigarette vapour Active CN209475918U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201822169261.2U CN209475918U (en) 2018-12-21 2018-12-21 The condensation water recovery and use system of high temperature cigarette vapour

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201822169261.2U CN209475918U (en) 2018-12-21 2018-12-21 The condensation water recovery and use system of high temperature cigarette vapour

Publications (1)

Publication Number Publication Date
CN209475918U true CN209475918U (en) 2019-10-11

Family

ID=68126834

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201822169261.2U Active CN209475918U (en) 2018-12-21 2018-12-21 The condensation water recovery and use system of high temperature cigarette vapour

Country Status (1)

Country Link
CN (1) CN209475918U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109453611A (en) * 2018-12-21 2019-03-12 江苏格陵兰传热科技有限公司 The condensation water recovery and use system of high temperature cigarette vapour

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109453611A (en) * 2018-12-21 2019-03-12 江苏格陵兰传热科技有限公司 The condensation water recovery and use system of high temperature cigarette vapour
CN109453611B (en) * 2018-12-21 2024-01-30 江苏格陵兰传热科技有限公司 Condensate recycling system for high-temperature flue gas

Similar Documents

Publication Publication Date Title
CN102506564B (en) Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system
CN103148644B (en) Microchannel falling-film evaporating condenser
CN203132218U (en) Evaporative condenser
CN102445066B (en) Natural air dehydrating and preheating drying oven system adopting condensate water waste heat for two-effect flash evaporation
CN104315875B (en) Power plant's spike cooling evaporative condenser
CN209475918U (en) The condensation water recovery and use system of high temperature cigarette vapour
CN205261805U (en) Evaporation formula condensing equipment based on separated heat pipe precooling
CN209295326U (en) Integrated countercurrent evaporation cooled water cooler
CN207975999U (en) Evaporative condenser easy to repair
CN109453611A (en) The condensation water recovery and use system of high temperature cigarette vapour
CN107381697A (en) A kind of high efficiency solar sea water desalinating unit
CN202485343U (en) Primary-effective flash natural air dehydrating, preheating and drying oven device by using condensate water waste heat
CN207210010U (en) A kind of high efficiency solar sea water desalinating unit
CN104964261A (en) Exhaust steam thermal energy recycling device
CN213739032U (en) Novel initiative recovery latent heat disk type solar energy sea water desalination device
CN108662915A (en) The indirect heat exchange vaporization type condensing system of the general vapour of concentration evaporator system end effect
CN205174937U (en) Sleeve pipe evaporative condenser with fin
CN206459524U (en) Pre-cooling type surface evaporation air cooler
CN210399571U (en) Absorption type refrigerator generator and refrigerator with same
CN209415849U (en) Except overheat evaporative condenser
CN200975844Y (en) Evaporative cooler
CN107651720B (en) Multistage humidification dehumidification type sea water desalination device with loop type gravity assisted heat pipe structure
CN208520224U (en) The indirect heat exchange vaporization type condensing system of the general vapour of concentration evaporator system end effect
CN207649433U (en) A kind of heat pipe evaporating condensation type heat exchanger
CN206593342U (en) A kind of efficient evaporating type condensing finned heat exchanger

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant