CN204372905U - Tobacco workshop steam utilization condensation water recovery system - Google Patents

Tobacco workshop steam utilization condensation water recovery system Download PDF

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Publication number
CN204372905U
CN204372905U CN201420714747.9U CN201420714747U CN204372905U CN 204372905 U CN204372905 U CN 204372905U CN 201420714747 U CN201420714747 U CN 201420714747U CN 204372905 U CN204372905 U CN 204372905U
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China
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water
valve
steam
recovery
recovery channel
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CN201420714747.9U
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Chinese (zh)
Inventor
王正伟
胡俊华
马楠
马飞
郭利民
许世勇
石峰
何保兵
詹旭
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河南中烟工业有限责任公司
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Abstract

Tobacco workshop steam utilization condensation water recovery system, comprises boiler (100), oxygen-eliminating device (101), softening water station (102), periodical blowdown expansion drum (103), high-temperature technology equipment (104), low temperature process equipment (105), combined air conditioner (106), flash tank (107), high pressure condensing hot air furnace tank (108), low pressure condensation water recovery tank (109), the first equipment for removing ferric ion (110) and the second equipment for removing ferric ion (111).The utility model becomes water to reclaim again into boiler from boiler output steam to steam-condensation, defines comparatively perfect closed cycle, is greatly improved by the recovery utilization rate of the heat of condensed water, water, flash steam, the pollution of not only having saved resource but also having decreased environment.

Description

Tobacco workshop steam utilization condensation water recovery system

Technical field

The utility model belongs to technical field of cigarette production, is specifically related to a kind of tobacco workshop steam utilization condensation water recovery system.

Background technology

The a lot of technology for making tobacco threds equipment of the vacuum conditioning, terrier, leaves moisting, flavoring and casing etc. of tobacco workshop needs to utilize in a large number that steam heats blade, pipe tobacco, humidification, and process equipment produces a large amount of condensed water in heating process.There is strict demand in Primary processing shop, storage silk room, wraparound workshop to ambient temperature and humidity, have installed a large amount of combined air conditioner unit, and combined air conditioner unit also produces a large amount of steam condensate (SC) after utilizing steam to promote environment temperature.Steam inlet tube also produces a large amount of condensed water owing to dispelling the heat in delivering vapor process.The condensate temperature discharged due to process equipment, combined air conditioner unit, steam inlet tube etc. is high and pure, and directly draining to affect environment, also causes heat energy and water resource waste.If recovery condensed water, because in process equipment, combined air conditioner, steam inlet tube, steam pressure is different, the condensed water pressure and temperature of discharge is different, like this when reclaiming condensed water, high pressure condensed water can hinder normal discharge and the recovery of low pressure condensed water, and traditional way of recycling can not reclaim condensed water completely, even if or reclaim the flash steam that condensed water but condensed water produce and emit, and water or flash steam can not be utilized completely.

Utility model content

The utility model, in order to solve weak point of the prior art, provides a kind of condensed water that can discharge process equipment, combined air conditioner and steam inlet tube to reclaim respectively and the tobacco workshop steam utilization condensation water recovery system recycled.

For solving the problems of the technologies described above, the utility model adopts following technical scheme: tobacco workshop steam utilization condensation water recovery system, comprises boiler 100, oxygen-eliminating device 101, softening water station 102, periodical blowdown expansion drum 103, high-temperature technology equipment 104, low temperature process equipment 105, combined air conditioner 106, flash tank 107, high pressure condensing hot air furnace tank 108, low pressure condensation water recovery tank 109, first equipment for removing ferric ion 110 and the second equipment for removing ferric ion 111;

The delivery port of softening water station 102 is connected with the water inlet of oxygen-eliminating device 101 by the first water pipe 117, first water pipe 117 is provided with the first water pump 36 and the first ball valve 37 successively along water (flow) direction, the delivery port of oxygen-eliminating device 101 is connected with the water inlet of boiler 100 by the second water pipe 118, and the second water pipe 118 is provided with the second water pump 33 and the second ball valve 34 successively along water (flow) direction;

The steam (vapor) outlet of boiler 100 is connected with the main inlet pipe 113 of steam, respectively by the first steam inlet tube 114 on the main inlet pipe 113 of steam, second steam inlet tube 115 and the 3rd steam inlet tube 116 and high-temperature technology equipment 104, low temperature process equipment 105 is connected with the air inlet of combined air conditioner 106, first steam inlet tube 114, second steam inlet tube 115 and the 3rd steam inlet tube 116 are respectively equipped with the first stop valve 3, second stop valve 6 and the 3rd stop valve 8, low temperature process equipment 105 is connected with the first filter 51 in flash tank 107 by the first recovery channel 119, the outlet of the first filter 51 is connected with the first impurity-discharging pipe 122 stretched out outside flash tank 107, first impurity-discharging pipe 122 is provided with the 4th ball valve 53, first recovery channel 119 is provided with the first drain valve group 7 of closing on low temperature process equipment 105 and the three or three ball valve 52 closing on flash tank 107, condensing hot air furnace pipe 120 is connected with between the main inlet pipe 113 of steam and the first recovery channel 119, condensing hot air furnace pipe 120 is provided with the second drain valve group 1, and the outlet of high-temperature technology equipment 104 is connected with the first recovery channel 119 by steam power steam trap connection,

The outlet of combined air conditioner 106 is connected with the second filter 17 in low pressure condensation water recovery tank 109 by the second recovery channel 121, second recovery channel 121 is provided with the 3rd drain valve group 9 of closing on combined air conditioner 106 and the 5th ball valve 16 closing on low pressure condensation water recovery tank 109, the outlet of the second filter 17 is connected with the second impurity-discharging pipe 123 stretched out outside low pressure condensation water recovery tank 109, second impurity-discharging pipe 123 is provided with the 6th ball valve 18, the outlet of low pressure condensation water recovery tank 109 is connected by the import of the 3rd recovery channel 124 with the second equipment for removing ferric ion 111, 3rd recovery channel 124 is provided with the 3rd water pump 20 and the 7th ball valve 21, the outlet of the second equipment for removing ferric ion 111 is connected with the 4th recovery channel 125, 4th recovery channel 125 is provided with the first electric three-way valve 25 closing on the second equipment for removing ferric ion 111,

The outlet of flash tank 107 is connected with the 3rd filter 45 in high pressure condensing hot air furnace tank 108 by the 5th recovery channel 126,5th recovery channel 126 is provided with the 8th ball valve 47 closing on high pressure condensing hot air furnace tank 108 and the 6th drain valve group 11 of closing on flash tank 107 and the 9th ball valve 10, the outlet of the 3rd filter 45 is connected with the 3rd impurity-discharging pipe the 137, three impurity-discharging pipe 137 stretched out outside high pressure condensing hot air furnace tank 108 and is provided with the tenth ball valve 12, the outlet of high pressure condensing hot air furnace tank 108 is connected by the import of the 6th recovery channel 138 with the first equipment for removing ferric ion 110, 6th recovery channel 138 is provided with the 4th water pump the 44 and the 11 ball valve 43, the outlet of the first equipment for removing ferric ion 110 is connected with the import of oxygen-eliminating device 101 by the 7th recovery channel 127, 7th recovery channel 127 is provided with the second electric three-way valve 29 closing on the first equipment for removing ferric ion 110 and the 12 ball valve 41 closing on oxygen-eliminating device 101, the outlet of the 4th recovery channel 125 is connected between the 12 ball valve 41 on the 7th recovery channel 127 and the second electric three-way valve 29, 3rd connector of the first electric three-way valve 25 and the second electric three-way valve 29 is foreign material outlet,

The impurity discharging port of boiler 100 is connected with the import of periodical blowdown expansion drum 103 by the 8th recovery channel 128, and the 8th recovery channel 128 is provided with the first magnetic valve 35.

Steam power steam trap connection comprises the first water leg 5, steam power drain valve pump 55 and the second water leg 54, the outlet of high-temperature technology equipment 104 is connected by the import of the 9th recovery channel 129 with the first water leg 5, 9th recovery channel 129 is provided with the 4th drain valve group 4, be connected by the first steam power pipe 130 between first steam inlet tube 114 with the second water leg 54, first steam power pipe 130 is provided with reducer unit 2, be connected by the second steam power pipe 131 between first steam power pipe 130 with steam power drain valve pump 55, second steam power pipe 131 is positioned at above the second water leg 54, be connected by the tenth recovery channel 132 between the delivery port of the second water leg 54 and the water inlet of the first water leg 5, tenth recovery channel 132 is provided with the 5th drain valve group 57, the delivery port of the first water leg 5 is connected by the 11 recovery channel 133 with the water inlet of steam power drain valve pump 55, 11 recovery channel 132 is provided with the 13 ball valve 58, the delivery port of steam power drain valve pump 55 is connected with the first recovery channel 119 by the 12 recovery channel 134, condensation balance pipe 135 is provided with between the top of steam power drain valve pump 55 and the top of the first water leg 5, condensation balance pipe 135 is provided with the 14 ball valve 56.

First recovery channel 119 is connected with the 5th recovery channel 126 and the second recovery channel 121 respectively by the 13 recovery channel 136, and the 13 recovery channel 136 is provided with the 15 ball valve 49 closing on the first recovery channel 119 and the 16 ball valve 13 closing on the second recovery channel 121.

Flash tank 107 top is connected with oxygen-eliminating device 101 by the 14 recovery channel 139,14 recovery channel 139 is provided with the two-way motor-driven valve 50 closing on flash tank 107 and the 17 ball valve 40 closing on oxygen-eliminating device 101, the bottom of high pressure condensing hot air furnace tank 108 is provided with the first blowoff valve 14, the top of high pressure condensing hot air furnace tank 108 is provided with first row blank pipe 140, first row blank pipe 140 is provided with first emptying valve 46, be connected with second row blank pipe 141 between first row blank pipe 140 and flash tank 107 top, second row blank pipe 141 is provided with second emptying valve 48.

First water pipe 117 is connected with backwash tube 143 between the first water pump 36 and the first ball valve 37, the outlet of backwash tube 143 is connected with the first equipment for removing ferric ion 110 and the second equipment for removing ferric ion 111 top respectively, backwash tube 143 be provided with close on the first water pipe 117 the 19 ball valve 38, close on the 20 ball valve 42 of the first equipment for removing ferric ion 110 and close on the 18 ball valve 23 of the second equipment for removing ferric ion 111.

Be connected with the 15 recovery channel 142 between the main inlet pipe 113 of steam and oxygen-eliminating device 117, the 15 recovery channel 142 is provided with the second magnetic valve 39.

The bottom of low pressure condensation water recovery tank 109 is provided with the second blowoff valve 19, and the top of low pressure condensation water recovery tank 109 is provided with the 3rd evacuated tube the 144, three evacuated tube 144 and is provided with the 3rd exhaust-valve 15.

Periodical blowdown expansion drum 103 top is provided with the 4th evacuated tube the 145, four evacuated tube 145 and is provided with the 4th exhaust-valve 32, and periodical blowdown expansion drum 103 top is connected with overflow pipe 30, is provided with the 3rd blowoff valve 31 bottom periodical blowdown expansion drum 103.

The bottom of the first equipment for removing ferric ion 110 and the second equipment for removing ferric ion 111 is respectively equipped with the 4th blowoff valve 26 and the 5th blowoff valve 22.

Adopt technique scheme, operation principle of the present utility model and the course of work as follows:

The steam pressure that boiler produces is about 1.0MPa, the steam that boiler produces flows to high-temperature technology equipment, low temperature process equipment, combined air conditioner through jet chimney, the main inlet pipe of steam is in delivering vapor process, because steam main inlet pipe length is longer, heat radiation can produce condensed water, condensed water in the main inlet pipe of steam exports through the second drain valve group, and the condensate temperature of output is more than 100 DEG C; Steam flows to high-temperature technology equipment through the first steam inlet tube, high-temperature technology equipment is low pressure gas utilization unit, steam is after the pressure-reducing valve that high-temperature technology equipment carries is depressurized to below 0.5MPa, export through the 4th drain valve group by being condensed into condensed water after high-temperature technology equipment heating pipe tobacco, the condensate temperature of output is more than 100 DEG C; Steam flows to low temperature process equipment through the second steam inlet tube, low temperature process equipment is high pressure gas utilization unit, be condensed into condensed water after the steam of 1.0MPa directly heats pipe tobacco in low temperature process equipment to export through the first drain valve group, the condensate temperature of output is more than 100 DEG C; Steam is depressurized to below 0.3MPa through reducer unit again through the 3rd steam inlet tube and flows to combined air conditioner, and the condensed water being condensed into less than 60 DEG C give air heat in combined air conditioner after exports through the 3rd drain valve group.Because the condensate temperature of the second drain valve group, the 4th drain valve group, the first drain valve group output is more than 100 DEG C, the condensate temperature that 3rd drain valve group exports is below 60 DEG C, two kinds of condensate temperatures and pressure gap larger, if through same recovery channel and condensate water recovery device, high-temp high-pressure condensation water can affect the discharge of low-temp low-pressure condensed water.Therefore the condensed water (condensed water that the main inlet pipe of steam, high-temperature technology equipment, low temperature process equipment produce) of more than 100 DEG C is reclaimed into a high pressure condensate water recovery device through a condensed water main pipeline (the first recovery channel), the condensed water (condensed water of combined air conditioner) of less than 60 DEG C reclaims into a low pressure condensate water recovery device through another root condensed water main pipeline (the second recovery channel) separately.

Pipeline after high-temperature condensation water pipeline i.e. the second drain valve group, the 4th drain valve group, the first drain valve group converges on first recovery channel, enter flash tank through the 3rd ball valve, the 15 ball valve, the 16 ball valve, first emptying valve, second emptying valve are closed at ordinary times.Flow to bottom flash tank after the first metre filter of flash tank.When first filter dirty more time, the 4th ball valve can be opened and drain dirty.Flash drum overhead is provided with two-way motor-driven valve, pressure setting opened by two-way motor-driven valve by control system is 0.06MPa, closing presure is set as 0.03MPa, when the pressure in flash tank is greater than 0.06 MPa, two-way motor-driven valve is opened automatically, the flash steam that high-temperature condensation water produces is through two-way motor-driven valve, the 17 ball valve again on the 14 recovery channel enters in oxygen-eliminating device the demineralized water heating oxygen-eliminating device, the flash steam that so not only high-temperature condensation water produces is utilized, and flash tank is by its top two-way motor-driven valve step-down, also the pressure in flash tank and condensate-water polishing pipeline is just reduced, avoid recovery system to sprain to press and impact to voltage process equipment, the normal discharge of low pressure process equipment and the main inlet pipe condensed water of steam.When the pressure of flash tank and condensate system is lower than 0.03 MPa, two-way motor-driven valve cuts out, pressure in such flash tank can ensure condensed water to compress into high pressure condensing hot air furnace tank through the 9th ball valve, the 6th drain valve group, the 8th ball valve, flows to high pressure condensing hot air furnace pot bottom after the 3rd metre filter of high pressure condensing hot air furnace tank.When the 3rd filter dirty more time, the tenth ball valve can be opened and drain dirty, and high pressure condensing hot air furnace pot bottom has the first blowoff valve.First emptying valve and second emptying valve are closed at ordinary times, and the 4th water pump controls according to the liquid level of high pressure condensing hot air furnace tank.The condensed water of high pressure condensing hot air furnace pot bottom is delivered to equipment for removing ferric ion by the 4th water pump through the 11 ball valve, and condensed water, after the first equipment for removing ferric ion removes iron ion and other impurity, enters the second electric three-way valve.Second electric three-way valve is connected with iron ion on-line computing model, and when the iron concentration after deironing reaches below normal concentration, the descending closedown of the second electric three-way valve, uply opens, and condensed water is crossed the second electric three-way valve and entered oxygen-eliminating device through the 12 ball valve.When iron concentration after condensed water deironing is still more than normal concentration, can not recycle, second electric three-way valve is descending to be opened, up closedown, condensed water is crossed the second electric three-way valve and is entered boiler periodical blowdown expansion drum, arrange into trench through the overflow pipe of periodical blowdown expansion drum after preliminary cooling in periodical blowdown expansion drum, drain into outdoor blowdown cooling tank through trench.

Although the condensate temperature that high-temperature technology equipment produces is more than 100 DEG C, but high-temperature technology equipment is low pressure gas utilization unit, the condensate temperature that the condensate temperature produced and pressure produce than the main inlet pipe of steam, low temperature process equipment etc. and pressure low, the condensed water of such low temperature process equipment and connecting pipe generation thereof may affect the normal discharge of high-temperature technology equipment condensed water.Therefore, after the 4th drain valve group of high-temperature technology equipment, install a set of steam power drain valve pump additional, steam power drain valve pump is equivalent to drain valve not having in dynamic situation.When the condensed water pressure after the 4th drain valve group is enough to the back pressure water delivery overcoming condensate water main pipeline, condensed water directly overcomes back pressure by steam power drain valve pump and exports.When the condensate water pressure after the 4th drain valve group can not overcome the back pressure water delivery of condensate water main pipeline, along with the rising of condensed water liquid level in steam power drain valve pump, inter-interlock mechanism action, steam is after reducer unit decompression, enter steam power drain valve pump to pressurize to condensed water, condensed water pressure is raised and overcomes pipeline back pressure, in steam power drain valve pump, condensed water is arranged into the first recovery channel.Before power steam enters steam power drain valve pump, power steam pipeline installs second water leg additional, the power steam quality entering steam power drain valve pump like this can be higher, avoids affecting water delivery.And the condensed water in the second water leg flows to the first water leg by the 5th drain valve group.14 ball valve and the pipeline installed are the condensation balance pipe of steam power drain valve pump, condensation balance pipe is used in equilibrium vapor power drain valve pump and pressure between anterior condensed water, avoids remaining vapour in steam power drain valve pump to affect anterior condensed water and flows in steam power drain valve pump.First water leg also plays the effect of the favourable water delivery of equalizing pressure.

Steam power drain valve pump also can according to high-temperature technology machine operation and the parallel connection of the 4th drain valve group, when the condensation water quantity of high-temperature technology equipment can overcome again pipeline back pressure comparatively greatly, condensed water can pass through the 4th drain valve group and the water delivery of steam power pump simultaneously, and conveyance power of water strengthens.Even if the condensed water pressure that high-temperature technology equipment produces can not overcome pipeline back pressure and export from the 4th drain valve group, power steam works, and also can be exported by steam power drain valve pump, and conveyance power of water is also larger when power steam is enabled.

First emptying valve near high pressure condensing hot air furnace tank, second emptying valve is closed at ordinary times, when the 8th ball vaeves failures of flash drum overhead can not be opened, or the steam in the main inlet pipe of steam leaks into condensate return system by the second drain valve group, 8th ball valve step-down is slower, during internal system hypertonia, can by first emptying valve, second emptying valve is opened, part flash steam is entered outdoor, part is recycled through threeway the 8th ball valve, realize quick pressure releasing condensate return system, reaching can not affect workshop because above reason hinders condensed water elimination and normally produce.

First emptying valve, second emptying valve, the 15 ball valve are closed at ordinary times, and condensing hot air furnace is enclosed condensation water recovery system.If flash tank breaks down, 15 ball valve can be opened, 3rd ball valve is closed, first emptying valve is opened, high-temperature condensation water pipeline i.e. the second drain valve group, 4th drain valve group, pipeline after first drain valve group converges on the 13 recovery channel, condensed water enters flash tank without the 3rd ball valve, but directly flow to high pressure condensing hot air furnace tank through the 15 ball valve and the 8th ball valve successively, high temperature flash steam is outside the direct discharge chamber of first emptying valve, become open type condensation water recovery system, even if thus flash tank fault also can not affect the condensing hot air furnace of process equipment.

The condensate temperature of combined air conditioner is generally below 60 DEG C, and temperature and pressure is all lower, if adopt same recovery channel and retracting device with more than 100 DEG C high-temp high-pressure condensation waters, high-temperature condensation water can affect the condensed water normal discharge of combined air conditioner.Therefore, the condensed water of combined air conditioner enters low pressure condensation water recovery tank through the 3rd drain valve group, the 5th ball valve, flow to bottom low pressure condensation water recovery tank after the second filter of low pressure condensation water recovery tank, when second filter dirty more time, the 6th ball valve can be opened and drain dirty.Condensed water in low pressure condensation water recovery tank is delivered to the second equipment for removing ferric ion by the 3rd water pump through the 7th ball valve, and condensed water enters the first electric three-way valve remove iron ion and other impurity in the second equipment for removing ferric ion after.First electric three-way valve is connected with iron ion on-line computing model, and when the iron concentration after deironing reaches below normal concentration, the descending closedown of the first electric three-way valve, uply opens, and condensed water is crossed the first electric three-way valve and entered oxygen-eliminating device through the 12 ball valve.When iron concentration after condensed water deironing is still more than normal concentration, can not recycle, first electric three-way valve is descending to be opened, up closedown, condensed water is crossed the first electric three-way valve and is entered boiler periodical blowdown expansion drum, overflow pipe again through boiler blow-off expansion drum is arranged into trench, drains into outdoor blowdown cooling tank through trench.

3rd exhaust-valve at low pressure condensation water recovery tank top is closed at ordinary times, system is enclosed condensation water recovery system, enter condensate return system when combined air conditioner has drain valve to lead directly to Lou vapour or have the by-passing valve of people's maloperation drain valve group to make steam enter condensation water recovery system, when causing condensation water recovery system pressure to raise, 3rd exhaust-valve can be opened, enclosed condensation water recovery system is become Recovery with Open-loop system, intrasystem pressure is discharged fast, thus does not affect the discharge of equipment condensed water and the recovery of condensed water.

16 ball valve is closed at ordinary times, the 16 ball valve can make high-temperature condensation water recycling can and cryogenic condensation water recovery tank for subsequent use each other, as long as opened by the exhaust-valve of the condensing hot air furnace tank top of one of them system, becoming Recovery with Open-loop system just can be for subsequent use each other.When high pressure condensing hot air furnace tank or the first equipment for removing ferric ion fault, 16 ball valve can be opened, 8th ball valve, the 3rd ball valve are closed, 3rd exhaust-valve is opened cryogenic condensation Water Sproading and becomes Recovery with Open-loop system, high-temperature condensation water directly enters low pressure condensation water recovery tank through the 15 ball valve, the 16 ball valve successively from the 13 recovery channel.Equally, when low pressure condensation water recovery tank or the second equipment for removing ferric ion fault, first emptying valve is opened high-temperature condensation water recovery and become Recovery with Open-loop system, low pressure condensed water enters high pressure condensing hot air furnace tank through the 16 ball valve and the 8th ball valve successively.

If the pressure reduction that control system detects equipment for removing ferric ion inside is comparatively large, what prove in equipment for removing ferric ion is dirty more, and the first equipment for removing ferric ion and the second equipment for removing ferric ion need regularly to utilize demineralized water to carry out backwash.When the first equipment for removing ferric ion backwash, the demineralized water of softening water station enters the first equipment for removing ferric ion through the 19 ball valve, the 20 ball valve successively by the first water pump, and the water of backwash enters trench through the 4th blowoff valve.When the second equipment for removing ferric ion backwash, the demineralized water of softening water station enters the second equipment for removing ferric ion through the 19 ball valve, the 18 ball valve successively by the first water pump, and the water of backwash enters trench through the 5th blowoff valve.If need automatically to control, only need to install electrically operated valve or operated pneumatic valve additional.

Oxygen-eliminating device be mainly boiler deoxygenation is provided after demineralized water.Oxygen-eliminating device deoxygenation is mainly by the Steam Heating of boiler.Boiler Steam by Cemented filling through the second magnetic valve to oxygen-eliminating device, the water of oxygen-eliminating device by after the second water pump pressurization through the second ball valve for boiler provides moisturizing.Therefore, flash steam can economize energy by the absorption of the water of oxygen-eliminating device.

Supply water to oxygen-eliminating device through the first ball valve after the demineralized water of softening water station is pressurizeed by water pump, the water of oxygen-eliminating device by after the second water pump pressurization through the second ball valve for boiler provides moisturizing.The steam that boiler produces gives the equipment such as oxygen-eliminating device, high-temperature technology equipment, low temperature process equipment, combined air conditioner through the main inlet pipe of steam, the condensed water that above equipment and pipeline produce reclaims into condensate water recovery device through drain valve group, condensed water, through the qualified laggard oxygen-eliminating device of deironing, then enters boiler develops steam vapor again.Material is thus formed the steam and condensate system of a circulation.After boiler blowdown water and deironing, still defective condensed water enters periodical blowdown expansion drum, and in blowdown expansion drum, after preliminary cooling, draining trench is entered in overflow, drains into outdoor blowdown cooling tank through trench.

In sum, high temperature and low temperature two kinds of condensed waters are divided into two system recoveries by the utility model, reclaimer can be for subsequent use each other, can closed-style recycling system be converted to Recovery with Open-loop system again when condensation water recovery system fault, flexibility and reliability improve greatly, overcome temperature, the different condensing hot air furnace difficult problem caused of pressure that different water delivery point exports condensed water.Because the utility model becomes water to reclaim again into boiler from boiler output steam to steam-condensation, define comparatively perfect closed cycle, the recovery utilization rate of the heat of condensed water, water, flash steam is improved greatly, the pollution of not only having saved resource but also having decreased environment.

Accompanying drawing explanation

Fig. 1 is structural representation of the present utility model.

Detailed description of the invention

As shown in Figure 1, tobacco workshop steam utilization condensation water recovery system of the present utility model, comprises boiler 100, oxygen-eliminating device 101, softening water station 102, periodical blowdown expansion drum 103, high-temperature technology equipment 104, low temperature process equipment 105, combined air conditioner 106, flash tank 107, high pressure condensing hot air furnace tank 108, low pressure condensation water recovery tank 109, first equipment for removing ferric ion 110 and the second equipment for removing ferric ion 111;

The delivery port of softening water station 102 is connected with the water inlet of oxygen-eliminating device 101 by the first water pipe 117, first water pipe 117 is provided with the first water pump 36 and the first ball valve 37 successively along water (flow) direction, the delivery port of oxygen-eliminating device 101 is connected with the water inlet of boiler 100 by the second water pipe 118, and the second water pipe 118 is provided with the second water pump 33 and the second ball valve 34 successively along water (flow) direction;

The steam (vapor) outlet of boiler 100 is connected with the main inlet pipe 113 of steam, respectively by the first steam inlet tube 114 on the main inlet pipe 113 of steam, second steam inlet tube 115 and the 3rd steam inlet tube 116 and high-temperature technology equipment 104, low temperature process equipment 105 is connected with the air inlet of combined air conditioner 106, first steam inlet tube 114, second steam inlet tube 115 and the 3rd steam inlet tube 116 are respectively equipped with the first stop valve 3, second stop valve 6 and the 3rd stop valve 8, low temperature process equipment 105 is connected with the first filter 51 in flash tank 107 by the first recovery channel 119, the outlet of the first filter 51 is connected with the first impurity-discharging pipe 122 stretched out outside flash tank 107, first impurity-discharging pipe 122 is provided with the 4th ball valve 53, first recovery channel 119 is provided with the first drain valve group 7 of closing on low temperature process equipment 105 and the three or three ball valve 52 closing on flash tank 107, condensing hot air furnace pipe 120 is connected with between the main inlet pipe 113 of steam and the first recovery channel 119, condensing hot air furnace pipe 120 is provided with the second drain valve group 1, and the outlet of high-temperature technology equipment 104 is connected with the first recovery channel 119 by steam power steam trap connection,

The outlet of combined air conditioner 106 is connected with the second filter 17 in low pressure condensation water recovery tank 109 by the second recovery channel 121, second recovery channel 121 is provided with the 3rd drain valve group 9 of closing on combined air conditioner 106 and the 5th ball valve 16 closing on low pressure condensation water recovery tank 109, the outlet of the second filter 17 is connected with the second impurity-discharging pipe 123 stretched out outside low pressure condensation water recovery tank 109, second impurity-discharging pipe 123 is provided with the 6th ball valve 18, the outlet of low pressure condensation water recovery tank 109 is connected by the import of the 3rd recovery channel 124 with the second equipment for removing ferric ion 111, 3rd recovery channel 124 is provided with the 3rd water pump 20 and the 7th ball valve 21, the outlet of the second equipment for removing ferric ion 111 is connected with the 4th recovery channel 125, 4th recovery channel 125 is provided with the first electric three-way valve 25 closing on the second equipment for removing ferric ion 111,

The outlet of flash tank 107 is connected with the 3rd filter 45 in high pressure condensing hot air furnace tank 108 by the 5th recovery channel 126,5th recovery channel 126 is provided with the 8th ball valve 47 closing on high pressure condensing hot air furnace tank 108 and the 6th drain valve group 11 of closing on flash tank 107 and the 9th ball valve 10, the outlet of the 3rd filter 45 is connected with the 3rd impurity-discharging pipe the 137, three impurity-discharging pipe 137 stretched out outside high pressure condensing hot air furnace tank 108 and is provided with the tenth ball valve 12, the outlet of high pressure condensing hot air furnace tank 108 is connected by the import of the 6th recovery channel 138 with the first equipment for removing ferric ion 110, 6th recovery channel 138 is provided with the 4th water pump the 44 and the 11 ball valve 43, the outlet of the first equipment for removing ferric ion 110 is connected with the import of oxygen-eliminating device 101 by the 7th recovery channel 127, 7th recovery channel 127 is provided with the second electric three-way valve 29 closing on the first equipment for removing ferric ion 110 and the 12 ball valve 41 closing on oxygen-eliminating device 101, the outlet of the 4th recovery channel 125 is connected between the 12 ball valve 41 on the 7th recovery channel 127 and the second electric three-way valve 29, 3rd connector of the first electric three-way valve 25 and the second electric three-way valve 29 is foreign material outlet,

The impurity discharging port of boiler 100 is connected with the import of periodical blowdown expansion drum 103 by the 8th recovery channel 128, and the 8th recovery channel 128 is provided with the first magnetic valve 35.

Steam power steam trap connection comprises the first water leg 5, steam power drain valve pump 55 and the second water leg 54, the outlet of high-temperature technology equipment 104 is connected by the import of the 9th recovery channel 129 with the first water leg 5, 9th recovery channel 129 is provided with the 4th drain valve group 4, be connected by the first steam power pipe 130 between first steam inlet tube 114 with the second water leg 54, first steam power pipe 130 is provided with reducer unit 2, be connected by the second steam power pipe 131 between first steam power pipe 130 with steam power drain valve pump 55, second steam power pipe 131 is positioned at above the second water leg 54, be connected by the tenth recovery channel 132 between the delivery port of the second water leg 54 and the water inlet of the first water leg 5, tenth recovery channel 132 is provided with the 5th drain valve group 57, the delivery port of the first water leg 5 is connected by the 11 recovery channel 133 with the water inlet of steam power drain valve pump 55, 11 recovery channel 132 is provided with the 13 ball valve 58, the delivery port of steam power drain valve pump 55 is connected with the first recovery channel 119 by the 12 recovery channel 134, condensation balance pipe 135 is provided with between the top of steam power drain valve pump 55 and the top of the first water leg 5, condensation balance pipe 135 is provided with the 14 ball valve 56.

First recovery channel 119 is connected with the 5th recovery channel 126 and the second recovery channel 121 respectively by the 13 recovery channel 136, and the 13 recovery channel 136 is provided with the 15 ball valve 49 closing on the first recovery channel 119 and the 16 ball valve 13 closing on the second recovery channel 121.

Flash tank 107 top is connected with oxygen-eliminating device 101 by the 14 recovery channel 139,14 recovery channel 139 is provided with the two-way motor-driven valve 50 closing on flash tank 107 and the 17 ball valve 40 closing on oxygen-eliminating device 101, the bottom of high pressure condensing hot air furnace tank 108 is provided with the first blowoff valve 14, the top of high pressure condensing hot air furnace tank 108 is provided with first row blank pipe 140, first row blank pipe 140 is provided with first emptying valve 46, be connected with second row blank pipe 141 between first row blank pipe 140 and flash tank 107 top, second row blank pipe 141 is provided with second emptying valve 48.

First water pipe 117 is connected with backwash tube 143 between the first water pump 36 and the first ball valve 37, the outlet of backwash tube 143 is connected with the first equipment for removing ferric ion 110 and the second equipment for removing ferric ion 111 top respectively, backwash tube 143 be provided with close on the first water pipe 117 the 19 ball valve 38, close on the 20 ball valve 42 of the first equipment for removing ferric ion 110 and close on the 18 ball valve 23 of the second equipment for removing ferric ion 111.

Be connected with the 15 recovery channel 142 between the main inlet pipe 113 of steam and oxygen-eliminating device 117, the 15 recovery channel 142 is provided with the second magnetic valve 39.

The bottom of low pressure condensation water recovery tank 109 is provided with the second blowoff valve 19, and the top of low pressure condensation water recovery tank 109 is provided with the 3rd evacuated tube the 144, three evacuated tube 144 and is provided with the 3rd exhaust-valve 15.

Periodical blowdown expansion drum 103 top is provided with the 4th evacuated tube the 145, four evacuated tube 145 and is provided with the 4th exhaust-valve 32, and periodical blowdown expansion drum 103 top is connected with overflow pipe 30, is provided with the 3rd blowoff valve 31 bottom periodical blowdown expansion drum 103.

Operation principle of the present utility model and the course of work as follows:

The steam pressure that boiler produces is about 1.0MPa, the steam that boiler produces flows to high-temperature technology equipment 104, low temperature process equipment 105, combined air conditioner 106 through jet chimney, the main inlet pipe 113 of steam is in delivering vapor process, because steam main inlet pipe 113 length is longer, heat radiation can produce condensed water, condensed water in the main inlet pipe 113 of steam exports through the second drain valve group 1, and the condensate temperature of output is more than 100 DEG C; Steam flows to high-temperature technology equipment 104 through the first steam inlet tube 114, high-temperature technology equipment 104 is low pressure gas utilization unit, steam is after the pressure-reducing valve that high-temperature technology equipment 104 carries is depressurized to below 0.5MPa, be condensed into condensed water after heating pipe tobacco by high-temperature technology equipment 104 to export through the 4th drain valve group 4, the condensate temperature of output is more than 100 DEG C; Steam flows to low temperature process equipment 105 through the second steam inlet tube 115, low temperature process equipment 105 is high pressure gas utilization unit, be condensed into condensed water after the steam of 1.0MPa directly heats pipe tobacco in low temperature process equipment 105 to export through the first drain valve group 7, the condensate temperature of output is more than 100 DEG C; Steam is depressurized to below 0.3MPa through reducer unit again through the 3rd steam inlet tube 116 and flows to combined air conditioner 106, and the condensed water being condensed into less than 60 DEG C give air heat in combined air conditioner 106 after exports through the 3rd drain valve group 9.Because the condensate temperature of the second drain valve group 1, the 4th drain valve group 4, first drain valve group 7 output is more than 100 DEG C, the condensate temperature that 3rd drain valve group 9 exports is below 60 DEG C, two kinds of condensate temperatures and pressure gap larger, if through same recovery channel and condensate water recovery device, high-temp high-pressure condensation water can affect the discharge of low-temp low-pressure condensed water.Therefore the condensed water (condensed water that the main inlet pipe 113 of steam, high-temperature technology equipment 104, low temperature process equipment 105 produce) of more than 100 DEG C is reclaimed into a high pressure condensate water recovery device through a condensed water main pipeline (the first recovery channel 119), the condensed water (condensed water of combined air conditioner 106) of less than 60 DEG C reclaims into a low pressure condensate water recovery device through another root condensed water main pipeline (the second recovery channel 121) separately.

Pipeline after high-temperature condensation water pipeline i.e. the second drain valve group 1, the 4th drain valve group 4, first drain valve group 7 converges on first recovery channel 119, enter flash tank 107 through the 3rd ball valve 52, close when the 15 ball valve the 49, the 16 ball valve 13, first emptying valve 46, second emptying valve 48 are flat.Flow to bottom flash tank 107 after the first filter 51 of flash tank 107 filters.When first filter 51 dirty more time, the 4th ball valve 53 can be opened and drain dirty.Flash tank 107 top is provided with two-way motor-driven valve 50, pressure setting opened by two-way motor-driven valve 50 by control system is 0.06MPa, closing presure is set as 0.03MPa, when the pressure in flash tank 107 is greater than 0.06 MPa, two-way motor-driven valve 50 is opened automatically, the flash steam that high-temperature condensation water produces is through two-way motor-driven valve 50, the 17 ball valve 40 again on the 14 recovery channel 139 enters the demineralized water heating oxygen-eliminating device 101 in oxygen-eliminating device 101, the flash steam that so not only high-temperature condensation water produces is utilized, and flash tank 107 is by its top two-way motor-driven valve 50 step-down, also the pressure in flash tank 107 and condensate-water polishing pipeline is just reduced, avoid recovery system to sprain to press and impact to voltage process equipment 104, the normal discharge of low pressure process equipment 105 and steam main inlet pipe 113 condensed water.When the pressure of flash tank 107 and condensate system is lower than 0.03 MPa, two-way motor-driven valve 50 cuts out, pressure in such flash tank 107 can ensure condensed water to compress into high pressure condensing hot air furnace tank 108 through the 9th ball valve 10, the 6th drain valve group 11, the 8th ball valve 47, flows to bottom high pressure condensing hot air furnace tank 108 after the 3rd filter 45 of high pressure condensing hot air furnace tank 108 filters.When the 3rd filter 45 dirty more time, the tenth ball valve 12 can be opened and drain dirty, and have the first blowoff valve 14 bottom high pressure condensing hot air furnace tank 108.First emptying valve 46 and second emptying valve 48 flat time close, the 4th water pump 44 controls according to the liquid level of high pressure condensing hot air furnace tank 108.Condensed water bottom high pressure condensing hot air furnace tank 108 is delivered to equipment for removing ferric ion 1 by the 4th water pump 44 through the 11 ball valve 43, and condensed water, after the first equipment for removing ferric ion 110 removes iron ion and other impurity, enters the second electric three-way valve 29.Second electric three-way valve 29 is connected with iron ion on-line computing model, when the iron concentration after deironing reaches below normal concentration, the descending closedown of second electric three-way valve 29, uply opens, and condensed water is crossed the second electric three-way valve 29 and entered oxygen-eliminating device 101 through the 12 ball valve 41.When iron concentration after condensed water deironing is still more than normal concentration, can not recycle, second electric three-way valve 29 is descending to be opened, up closedown, condensed water is crossed the second electric three-way valve 29 and is entered boiler periodical blowdown expansion drum 103, arrange into trench through the overflow pipe 30 of periodical blowdown expansion drum 103 after preliminary cooling in periodical blowdown expansion drum 103, drain into outdoor blowdown cooling tank through trench.

Although the condensate temperature that high-temperature technology equipment 104 produces is more than 100 DEG C, but high-temperature technology equipment 104 is low pressure gas utilization units, the condensate temperature that the condensate temperature produced and pressure produce than the main inlet pipe of steam 113, low temperature process equipment 105 etc. and pressure low, the condensed water of such low temperature process equipment 105 and connecting pipe generation thereof may affect the normal discharge of high-temperature technology equipment 104 condensed water.Therefore, after the 4th drain valve group 4 of high-temperature technology equipment 104, install a set of steam power drain valve pump 55 additional, steam power drain valve pump 55 is equivalent to drain valve not having in dynamic situation.When the condensed water pressure after the 4th drain valve group 4 is enough to the back pressure water delivery overcoming condensate water main pipeline, condensed water directly overcomes back pressure by steam power drain valve pump 55 and exports.When the condensate water pressure after the 4th drain valve group 4 can not overcome the back pressure water delivery of condensate water main pipeline, along with the rising of condensed water liquid level in steam power drain valve pump 55, inter-interlock mechanism action, steam is after reducer unit 2 reduces pressure, enter steam power drain valve pump 55 to pressurize to condensed water, condensed water pressure is raised and overcomes pipeline back pressure, in steam power drain valve pump 55, condensed water is arranged into the first recovery channel 119.Before power steam enters steam power drain valve pump 55, power steam pipeline installs additional second water leg 54, and the power steam quality entering steam power drain valve pump 55 like this can be higher, avoids affecting water delivery.And the condensed water in the second water leg 54 flows to the first water leg 5 by the 5th drain valve group 57.14 ball valve 56 and the pipeline installed are the condensation balance pipe 135 of steam power drain valve pump 55, condensation balance pipe is used for the pressure in equilibrium vapor power drain valve pump 55 and between anterior condensed water, avoids remaining vapour in steam power drain valve pump 55 to affect anterior condensed water and flows in steam power drain valve pump 55.First water leg 5 also plays the effect of the favourable water delivery of equalizing pressure.

Steam power drain valve pump 55 also can according to high-temperature technology equipment 104 ruuning situation and the parallel connection of the 4th drain valve group 4, when the condensation water quantity of high-temperature technology equipment 104 can overcome again pipeline back pressure comparatively greatly, condensed water can pass through the 4th drain valve group 4 and the water delivery of steam power pump simultaneously, and conveyance power of water strengthens.Even if the condensed water pressure that high-temperature technology equipment 104 produces can not overcome pipeline back pressure and export from the 4th drain valve group 4, power steam works, and also can be exported by steam power drain valve pump 55, and conveyance power of water is also larger when power steam is enabled.

First emptying valve 46 near high pressure condensing hot air furnace tank 108, close when second emptying valve 48 is flat, the 8th ball valve 47 fault when flash tank 107 top can not be opened, or the steam in the main inlet pipe 113 of steam leaks into condensate return system by the second drain valve group 1, 8th ball valve 47 step-down is slower, during internal system hypertonia, can by first emptying valve 46, second emptying valve 48 is opened, part flash steam is entered outdoor, part is recycled through threeway the 8th ball valve 47, realize quick pressure releasing condensate return system, reaching can not affect workshop because above reason hinders condensed water elimination and normally produce.

Close when first emptying valve 46, second emptying valve the 48, the 15 ball valve 49 are flat, condensing hot air furnace is enclosed condensation water recovery system.If flash tank 107 breaks down, 15 ball valve 49 can be opened, 3rd ball valve 52 is closed, first emptying valve 46 is opened, high-temperature condensation water pipeline i.e. the second drain valve group 1, 4th drain valve group 4, pipeline after first drain valve group 7 converges on the 13 recovery channel 136, condensed water enters flash tank 107 without the 3rd ball valve 52, but directly flow to high pressure condensing hot air furnace tank 108 through the 15 ball valve 49 and the 8th ball valve 47 successively, high temperature flash steam is outside first emptying valve 46 directly discharge chamber, become open type condensation water recovery system, even if thus flash tank 107 fault also can not affect the condensing hot air furnace of process equipment.

The condensate temperature of combined air conditioner 106 is generally below 60 DEG C, and temperature and pressure is all lower, if adopt same recovery channel and retracting device with more than 100 DEG C high-temp high-pressure condensation waters, high-temperature condensation water can affect the condensed water normal discharge of combined air conditioner 106.Therefore, the condensed water of combined air conditioner 106 enters low pressure condensation water recovery tank 109 through the 3rd drain valve group 9, the 5th ball valve 16, flow to bottom low pressure condensation water recovery tank 109 after the second filter 17 of low pressure condensation water recovery tank 109, when second filter 17 dirty more time, the 6th ball valve 18 can be opened and drain dirty.Condensed water in low pressure condensation water recovery tank 109 is delivered to the second equipment for removing ferric ion 111 by the 3rd water pump 20 through the 7th ball valve 21, and condensed water enters the first electric three-way valve 25 remove iron ion and other impurity in the second equipment for removing ferric ion 111 after.First electric three-way valve 25 is connected with iron ion on-line computing model, when the iron concentration after deironing reaches below normal concentration, the descending closedown of first electric three-way valve 25, uply opens, and condensed water is crossed the first electric three-way valve 25 and entered oxygen-eliminating device 101 through the 12 ball valve 41.When iron concentration after condensed water deironing is still more than normal concentration, can not recycle, first electric three-way valve 25 is descending to be opened, up closedown, condensed water is crossed the first electric three-way valve 25 and is entered boiler periodical blowdown expansion drum 103, overflow pipe 30 again through boiler blow-off expansion drum is arranged into trench, drains into outdoor blowdown cooling tank through trench.

Close when 3rd exhaust-valve 15 at low pressure condensation water recovery tank 109 top is flat, system is enclosed condensation water recovery system, enter condensate return system when combined air conditioner 106 has drain valve to lead directly to Lou vapour or have the by-passing valve of people's maloperation drain valve group to make steam enter condensation water recovery system, when causing condensation water recovery system pressure to raise, 3rd exhaust-valve 15 can be opened, enclosed condensation water recovery system is become Recovery with Open-loop system, intrasystem pressure is discharged fast, thus does not affect the discharge of equipment condensed water and the recovery of condensed water.

Close when 16 ball valve 13 is flat, 16 ball valve 13 can make high-temperature condensation water recycling can 108 and cryogenic condensation water recovery tank 109 for subsequent use each other, as long as opened by the exhaust-valve of the condensing hot air furnace tank top of one of them system, becoming Recovery with Open-loop system just can be for subsequent use each other.When high pressure condensing hot air furnace tank 108 or the first equipment for removing ferric ion 110 fault, 16 ball valve 13 can be opened, 8th ball valve 47, the 3rd ball valve 52 are closed, 3rd exhaust-valve 15 is opened cryogenic condensation Water Sproading and becomes Recovery with Open-loop system, high-temperature condensation water directly enters low pressure condensation water recovery tank 109 through the 15 ball valve the 49, the 16 ball valve 13 successively from the 13 recovery channel 136.Equally, when low pressure condensation water recovery tank 109 or the second equipment for removing ferric ion 111 fault, first emptying valve 46 is opened high-temperature condensation water recovery and become Recovery with Open-loop system, low pressure condensed water enters high pressure condensing hot air furnace tank 108 through the 16 ball valve 13 and the 8th ball valve 47 successively.

If the pressure reduction that control system detects equipment for removing ferric ion inside is comparatively large, what prove in equipment for removing ferric ion is dirty more, and the first equipment for removing ferric ion 110 and the second equipment for removing ferric ion 111 need regularly to utilize demineralized water to carry out backwash.When the first equipment for removing ferric ion 110 backwash, the demineralized water of softening water station 102 enters the first equipment for removing ferric ion 110 through the 19 ball valve the 38, the 20 ball valve 42 successively by the first water pump 36, and the water of backwash enters trench through the 4th blowoff valve 26.When the second equipment for removing ferric ion 111 backwash, the demineralized water of softening water station 102 enters the second equipment for removing ferric ion 111 through the 19 ball valve the 38, the 18 ball valve 23 successively by the first water pump 36, and the water of backwash enters trench through the 5th blowoff valve 22.If need automatically to control, only need to install electrically operated valve or operated pneumatic valve additional.

Oxygen-eliminating device 101 be mainly boiler deoxygenation is provided after demineralized water.Oxygen-eliminating device 101 deoxygenation is mainly by the Steam Heating of boiler 100.Boiler 100 steam by Cemented filling through the second magnetic valve 39 to oxygen-eliminating device 101, after the water of oxygen-eliminating device 101 is pressurizeed by the second water pump 33 through the second ball valve 34 for boiler 100 provides moisturizing.Therefore, flash steam can economize energy by the absorption of the water of oxygen-eliminating device 101.

Supply water to oxygen-eliminating device 101 through the first ball valve 37 after the demineralized water of softening water station 102 is pressurizeed by water pump 36, after the water of oxygen-eliminating device 101 is pressurizeed by the second water pump 33 through the second ball valve 34 for boiler 100 provides moisturizing.The steam that boiler 100 produces gives the equipment such as oxygen-eliminating device 101, high-temperature technology equipment 104, low temperature process equipment 105, combined air conditioner 106 through the main inlet pipe 113 of steam, the condensed water that above equipment and pipeline produce reclaims into condensate water recovery device through drain valve group, condensed water, through the qualified laggard oxygen-eliminating device 101 of deironing, then enters again boiler 100 and produces steam.Material is thus formed the steam and condensate system of a circulation.After boiler 100 sewer and deironing, still defective condensed water enters periodical blowdown expansion drum 103, and in blowdown expansion drum, after preliminary cooling, draining trench is entered in overflow, drains into outdoor blowdown cooling tank through trench.

Above embodiment is the unrestricted the technical solution of the utility model in order to explanation only, although be described in detail the utility model with reference to above-described embodiment, those of ordinary skill in the art is to be understood that: still can modify to the utility model or equivalent replacement, and not departing from any modification or partial replacement of spirit and scope of the present utility model, it all should be encompassed in the middle of right of the present utility model.

Claims (9)

1. tobacco workshop steam utilization condensation water recovery system, is characterized in that: comprise boiler (100), oxygen-eliminating device (101), softening water station (102), periodical blowdown expansion drum (103), high-temperature technology equipment (104), low temperature process equipment (105), combined air conditioner (106), flash tank (107), high pressure condensing hot air furnace tank (108), low pressure condensation water recovery tank (109), the first equipment for removing ferric ion (110) and the second equipment for removing ferric ion (111);
The delivery port of softening water station (102) is connected with the water inlet of oxygen-eliminating device (101) by the first water pipe (117), first water pipe (117) is provided with the first water pump (36) and the first ball valve (37) successively along water (flow) direction, the delivery port of oxygen-eliminating device (101) is connected with the water inlet of boiler (100) by the second water pipe (118), and the second water pipe (118) is provided with the second water pump (33) and the second ball valve (34) successively along water (flow) direction;
The steam (vapor) outlet of boiler (100) is connected with the main inlet pipe of steam (113), respectively by the first steam inlet tube (114) on the main inlet pipe of steam (113), second steam inlet tube (115) and the 3rd steam inlet tube (116) and high-temperature technology equipment (104), low temperature process equipment (105) is connected with the air inlet of combined air conditioner (106), first steam inlet tube (114), second steam inlet tube (115) and the 3rd steam inlet tube (116) are respectively equipped with the first stop valve (3), second stop valve (6) and the 3rd stop valve (8), low temperature process equipment (105) is connected with the first filter (51) in flash tank (107) by the first recovery channel (119), the outlet of the first filter (51) is connected with stretches out flash tank (107) the first impurity-discharging pipe (122) outward, first impurity-discharging pipe (122) is provided with the 4th ball valve (53), first recovery channel (119) is provided with the first drain valve group (7) of closing on low temperature process equipment (105) and the 3rd ball valve (52) closing on flash tank (107), condensing hot air furnace pipe (120) is connected with between the main inlet pipe of steam (113) and the first recovery channel (119), condensing hot air furnace pipe (120) is provided with the second drain valve group (1), and the outlet of high-temperature technology equipment (104) is connected with the first recovery channel (119) by steam power steam trap connection,
The outlet of combined air conditioner (106) is connected with the second filter (17) in low pressure condensation water recovery tank (109) by the second recovery channel (121), second recovery channel (121) is provided with the 3rd drain valve group (9) of closing on combined air conditioner (106) and the 5th ball valve (16) closing on low pressure condensation water recovery tank (109), the outlet of the second filter (17) is connected with stretches out low pressure condensation water recovery tank (109) the second impurity-discharging pipe (123) outward, second impurity-discharging pipe (123) is provided with the 6th ball valve (18), the outlet of low pressure condensation water recovery tank (109) is connected with the import of the second equipment for removing ferric ion (111) by the 3rd recovery channel (124), 3rd recovery channel (124) is provided with the 3rd water pump (20) and the 7th ball valve (21), the outlet of the second equipment for removing ferric ion (111) is connected with the 4th recovery channel (125), 4th recovery channel (125) is provided with the first electric three-way valve (25) closing on the second equipment for removing ferric ion (111),
The outlet of flash tank (107) is connected with the 3rd filter (45) in high pressure condensing hot air furnace tank (108) by the 5th recovery channel (126), 5th recovery channel (126) is provided with the 8th ball valve (47) closing on high pressure condensing hot air furnace tank (108) and the 6th drain valve group (11) of closing on flash tank (107) and the 9th ball valve (10), the outlet of the 3rd filter (45) is connected with stretches out high pressure condensing hot air furnace tank (108) the 3rd impurity-discharging pipe (137) outward, and the 3rd impurity-discharging pipe (137) is provided with the tenth ball valve (12), the outlet of high pressure condensing hot air furnace tank (108) is connected with the import of the first equipment for removing ferric ion (110) by the 6th recovery channel (138), 6th recovery channel (138) is provided with the 4th water pump (44) and the 11 ball valve (43), the outlet of the first equipment for removing ferric ion (110) is connected with the import of oxygen-eliminating device (101) by the 7th recovery channel (127), 7th recovery channel (127) is provided with the second electric three-way valve (29) closing on the first equipment for removing ferric ion (110) and the 12 ball valve (41) closing on oxygen-eliminating device (101), the outlet of the 4th recovery channel (125) is connected between the 12 ball valve (41) on the 7th recovery channel (127) and the second electric three-way valve (29), 3rd connector of the first electric three-way valve (25) and the second electric three-way valve (29) is foreign material outlet,
The impurity discharging port of boiler (100) is connected with the import of periodical blowdown expansion drum (103) by the 8th recovery channel (128), and the 8th recovery channel (128) is provided with the first magnetic valve (35).
2. tobacco workshop steam utilization condensation water recovery system according to claim 1, it is characterized in that: described steam power steam trap connection comprises the first water leg (5), steam power drain valve pump (112) and the second water leg (54), the outlet of high-temperature technology equipment (104) is connected with the import of the first water leg (5) by the 9th recovery channel (129), 9th recovery channel (129) is provided with the 4th drain valve group (4), be connected by the first steam power pipe (130) between first steam inlet tube (114) with the second water leg (54), first steam power pipe (130) is provided with reducer unit (2), first steam power pipe (130) is connected by the second steam power pipe (131) with between steam power drain valve pump (112), second steam power pipe (131) is positioned at the second water leg (54) top, be connected by the tenth recovery channel (132) between the delivery port of the second water leg (54) and the water inlet of the first water leg (5), tenth recovery channel (132) is provided with the 5th drain valve group (57), the delivery port of the first water leg (5) is connected by the 11 recovery channel (133) with the water inlet of steam power drain valve pump (112), 11 recovery channel (132) is provided with the 13 ball valve (58), the delivery port of steam power drain valve pump (112) is connected with the first recovery channel (119) by the 12 recovery channel (134), condensation balance pipe (135) is provided with between the top of steam power drain valve pump (112) and the top of the first water leg (5), condensation balance pipe (135) is provided with the 14 ball valve (56).
3. tobacco workshop steam utilization condensation water recovery system according to claim 1 and 2, it is characterized in that: described first recovery channel (119) is connected with the 5th recovery channel (126) and the second recovery channel (121) respectively by the 13 recovery channel (136), the 13 recovery channel (136) is provided with the 15 ball valve (49) closing on the first recovery channel (119) and the 16 ball valve (13) closing on the second recovery channel (121).
4. tobacco workshop steam utilization condensation water recovery system according to claim 1 and 2, it is characterized in that: described flash tank (107) top is connected with oxygen-eliminating device (101) by the 14 recovery channel (139), 14 recovery channel (139) is provided with the two-way motor-driven valve (50) closing on flash tank (107) and the 17 ball valve (40) closing on oxygen-eliminating device (101), the bottom of high pressure condensing hot air furnace tank (108) is provided with the first blowoff valve (14), the top of high pressure condensing hot air furnace tank (108) is provided with first row blank pipe (140), first row blank pipe (140) is provided with first emptying valve (46), second row blank pipe (141) is connected with between first row blank pipe (140) and flash tank (107) top, second row blank pipe (141) is provided with second emptying valve (48).
5. tobacco workshop steam utilization condensation water recovery system according to claim 1 and 2, it is characterized in that: described first water pipe (117) is connected with backwash tube (143) between the first water pump (36) and the first ball valve (37), the outlet of backwash tube (143) is connected with the first equipment for removing ferric ion (110) and the second equipment for removing ferric ion (111) top respectively, backwash tube (143) is provided with the 19 ball valve (38) closing on the first water pipe (117), close on the 20 ball valve (42) of the first equipment for removing ferric ion (110) and close on the 18 ball valve (23) of the second equipment for removing ferric ion (111).
6. tobacco workshop steam utilization condensation water recovery system according to claim 1 and 2, it is characterized in that: be connected with the 15 recovery channel (142) between the main inlet pipe of described steam (113) and oxygen-eliminating device (117), the 15 recovery channel (142) is provided with the second magnetic valve (39).
7. tobacco workshop steam utilization condensation water recovery system according to claim 1 and 2, it is characterized in that: the bottom of described low pressure condensation water recovery tank (109) is provided with the second blowoff valve (19), the top of low pressure condensation water recovery tank (109) is provided with the 3rd evacuated tube (144), and the 3rd evacuated tube (144) is provided with the 3rd exhaust-valve (15).
8. tobacco workshop steam utilization condensation water recovery system according to claim 1 and 2, it is characterized in that: described periodical blowdown expansion drum (103) top is provided with the 4th evacuated tube (145), 4th evacuated tube (145) is provided with the 4th exhaust-valve (32), periodical blowdown expansion drum (103) top is connected with overflow pipe (30), and periodical blowdown expansion drum (103) bottom is provided with the 3rd blowoff valve (31).
9. tobacco workshop steam utilization condensation water recovery system according to claim 1 and 2, is characterized in that: the bottom of described first equipment for removing ferric ion (110) and the second equipment for removing ferric ion (111) is respectively equipped with the 4th blowoff valve (26) and the 5th blowoff valve (22).
CN201420714747.9U 2014-11-25 2014-11-25 Tobacco workshop steam utilization condensation water recovery system CN204372905U (en)

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Application Number Priority Date Filing Date Title
CN201420714747.9U CN204372905U (en) 2014-11-25 2014-11-25 Tobacco workshop steam utilization condensation water recovery system

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Application Number Priority Date Filing Date Title
CN201420714747.9U CN204372905U (en) 2014-11-25 2014-11-25 Tobacco workshop steam utilization condensation water recovery system

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Publication Number Publication Date
CN204372905U true CN204372905U (en) 2015-06-03

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CN201420714747.9U CN204372905U (en) 2014-11-25 2014-11-25 Tobacco workshop steam utilization condensation water recovery system

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104501130A (en) * 2014-11-25 2015-04-08 河南中烟工业有限责任公司 Steam-utilizing condensate water recycling system for cut tobacco production workshop of cigarette factory
CN105972987A (en) * 2016-05-27 2016-09-28 福建省闽清双棱竹业有限公司 Steam cyclic utilization system of manufacturing workshop for container floors
CN107490001A (en) * 2017-08-04 2017-12-19 河南中烟工业有限责任公司 A kind of condensation water recovery and use system

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104501130A (en) * 2014-11-25 2015-04-08 河南中烟工业有限责任公司 Steam-utilizing condensate water recycling system for cut tobacco production workshop of cigarette factory
CN104501130B (en) * 2014-11-25 2016-06-01 河南中烟工业有限责任公司 Tobacco workshop steam utilization condensate recovery system
CN105972987A (en) * 2016-05-27 2016-09-28 福建省闽清双棱竹业有限公司 Steam cyclic utilization system of manufacturing workshop for container floors
CN105972987B (en) * 2016-05-27 2018-11-23 福建省闽清双棱竹业有限公司 A kind of container floor manufacturing shop steam recycling system
CN107490001A (en) * 2017-08-04 2017-12-19 河南中烟工业有限责任公司 A kind of condensation water recovery and use system

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