CN103088510B - Non-return-air classification heat exchange dewatering and air exhaust waste heat utilization relaxation heat setting machine - Google Patents
Non-return-air classification heat exchange dewatering and air exhaust waste heat utilization relaxation heat setting machine Download PDFInfo
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- CN103088510B CN103088510B CN201310025605.1A CN201310025605A CN103088510B CN 103088510 B CN103088510 B CN 103088510B CN 201310025605 A CN201310025605 A CN 201310025605A CN 103088510 B CN103088510 B CN 103088510B
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Abstract
The invention relates to a non-return-air classification heat exchange dewatering and air exhaust waste heat utilization relaxation heat setting machine. An exhaust outlet is formed in the lower portion of a drying chamber, the exhaust outlet is communicated to the outside of a box body through an exhaust tube, an air compensation port in the box body is communicated with a suction port of a fan, an air outlet of the fan is aligned to heat exchangers above the fan, the air outlet above the heat exchangers enters into the drying chamber, an inlet of a high pressure heat exchanger is connected with a steam supply main tube, an outlet of a high pressure drain valve of the high pressure heat exchanger is connected into an inlet of a middle pressure heat exchanger through a first condensate water reuse tube, an outlet of a middle pressure drain valve of the middle pressure heat exchanger is connected into an inlet of a lower pressure heat exchanger through a second condensate water reuse tube, an outlet of the low pressure heat exchanger is connected into a condensate pump through a low pressure drain valve, a preheating air outlet of a new wind preheater is connected into the air compensation port of the relaxation setting machine, and exhaust of the relaxation setting machine is connected into the new wind preheater to achieve indirect heat exchange with new wind. The setting machine can achieve sufficient utilization of waste heat of the exhaust and condensate water, and is high in heat efficiency.
Description
Technical field
The present invention relates to a kind of loosening heat setting machine, particularly a kind of without return air classification heat exchange, hydrophobic and air exhaust waste heat utilizes loosening heat setting machine.
Background technology
The post processing of polyester staple fiber often uses loosening heat setting machine, the cabinets cavity of loosening heat setting machine is provided with blower fan, heat exchanger and product is carried out to the drying chamber of shaping and drying, the inlet scoop of blower fan communicates with the wind-supplying mouth on casing, the air outlet of blower fan aims at the heat exchanger of top, air outlet above heat exchanger enters drying chamber, is provided with exhaust outlet below drying chamber, and exhaust outlet leads to outside casing by exhaust duct, exhaust duct is provided with hand control valve, and return air inlet also communicates with the inlet scoop of blower fan.Heat exchanger is blowed to through blower fan after the new wind entered in casing from wind-supplying mouth mixes with return air, heat exchanger is heated becomes hot blast, hot blast enters drying chamber and shapes to product and dry, and then a part of wind enters exhaust outlet by air draft, and a part of wind is by return air inlet reuse.High-pressure steam pipe, middle pressure steam pipe are connected with main feed header respectively by stop valve with low pressure steam pipe, and main feed header is connected with the entrance of heat exchanger, and the outlet conduit of heat exchanger is provided with drain valve.
The weak point of this loosening heat setting machine is: (1) is different according to product, Three Estate is had with steam pressure, but only a drain valve is installed, drain valve normally can only work under some pressure, when non-design pressure state, can not maintain the pressure reduction needed for normal work, or discharge capacity is inadequate, or steam leakage is serious.(2) drain valve arrange condensed water waste heat need external user to be used, when without suitable user, be inevitably drained waste.(3) pollutant that return air carries very easily deposits at heat exchanger, worsens heat exchange efficiency.(4) even if condensation water residual heat is flashed utilization, the condensate temperature of discharge still has 130 DEG C ~ 150 DEG C, and waste heat loss measures greatly.(5) high temperature air exhaust waste heat does not utilize, exhaust air rate Non-follow control, and discharge capacity randomness is large.
Summary of the invention
The object of the invention is to, overcome problems of the prior art, there is provided that a kind of hydrophobic and air exhaust waste heat utilizes loosening heat setting machine without return air classification heat exchange, no matter product use high pressure or middle pressure steam, loosening heat setting machine self all can realize waste heat step, make full use of.
For solving above technical problem, it is of the present invention that a kind of without return air classification heat exchange, hydrophobic and air exhaust waste heat utilizes loosening heat setting machine, the cabinets cavity of loosening heat setting machine is provided with blower fan, heat exchanger and product is carried out to the drying chamber of shaping and drying, the inlet scoop of described blower fan communicates with the wind-supplying mouth on casing, the air outlet of blower fan aims at the heat exchanger of top, air outlet above described heat exchanger enters described drying chamber, exhaust outlet is provided with below drying chamber, described exhaust outlet leads to outside casing by exhaust duct, also comprise fresh air preheating device, the below of described fresh air preheating device is provided with new wind entrance, the top of fresh air preheating device is provided with pre-hot-blast outlet, the exhaust duct access fresh air preheating device of loosening heat setting machine makes air draft and new wind carry out indirect heat exchange, the described wind-supplying mouth of the pre-hot-blast outlet access loosening heat setting machine of described fresh air preheating device, described heat exchanger comprises high pressure heat exchanger stacked successively from top to bottom, middle pressure heat exchanger and low pressure heat exchanger, the entrance of described high pressure heat exchanger is connected with main feed header, the outlet access high pressure drain valve of described high pressure heat exchanger, the outlet of described high pressure drain valve accesses the entrance of described middle pressure heat exchanger by the first recycling condensing water pipe, drain valve is pressed in the outlet access of middle pressure heat exchanger, the outlet of middle pressure drain valve accesses the entrance of described low pressure heat exchanger by the second recycling condensing water pipe, low pressure heat exchanger exit is by low pressure drain valve access condensate pump.
Relative to prior art, the present invention achieves following beneficial effect: (1) drying chamber participates in circulation without return air, avoids the incrustation of return air entrainment heat exchanger surface in setting machine, adds heat exchange efficiency, extends the time between overhauls(TBO), (2) the air draft access fresh air preheating device of loosening heat setting machine carries out preheating to new wind, waste heat in air draft is recovered, decrease thermal pollution and the heat loss of discharge, new air temperature is improved in rear feeding loosening heat setting machine, reduces the steam consumption of heat exchanger in loosening heat setting machine, (3) traditional single heat exchanger is divided into high pressure heat exchanger stacked successively from top to bottom, middle pressure heat exchanger and low pressure heat exchanger, when Product Process needs high steam, only need to high pressure heat exchanger steam supply wherein, high steam becomes high pressure condensed water discharge latent heat in high pressure heat exchanger after, high pressure condensed water enters middle pressure heat exchanger after being dredged out by high pressure drain valve, in the flash distillation due to dilatation of middle pressure heat exchanger mesohigh condensed water, condensed water pressure drop, flash steam and air heat-exchange be rapid condensation after discharging latent heat, non-flash distillation and the condensed water of the condensed water of pressure drop and time condensation presses condensed water therefrom to press drain valve to dredge out in becoming continue to discharge sensible heat in middle pressure heat exchanger after, middle pressure drain valve presses the flow of condensed water to ensure condensed water and the sufficient exchange heat of pre-hot blast in controlling, middle pressure condensed water is dredged out by middle pressure drain valve and is entered low pressure heat exchanger, in low pressure heat exchanger, the flash distillation again due to dilatation of middle pressure condensed water, condensed water pressure declines further, flash steam and air heat-exchange be rapid condensation after discharging latent heat, become low pressure condensed water after the condensed water of the condensed water that non-flash distillation and pressure decline further and three condensations continues to discharge sensible heat in low pressure heat exchanger to dredge out from low pressure drain valve, low pressure drain valve controls the flow of low pressure condensed water to ensure condensed water and the sufficient exchange heat of pre-hot blast, (4) when Product Process needs to use middle pressure steam, high pressure heat exchanger and middle pressure heat exchanger all use the middle pressure steam of outer confession, drain valve is pressed to enter low pressure heat exchanger in the middle pressure condensed water warp that high pressure heat exchanger and middle pressure heat exchanger produce, in low pressure heat exchanger, the flash distillation due to dilatation of middle pressure condensed water, condensed water pressure drop, condensation rapidly after flash steam release latent heat, non-flash distillation and the condensed water of the condensed water of pressure drop and time condensation becomes low pressure condensed water continue to discharge sensible heat in low pressure heat exchanger after dredges out from low pressure drain valve, low pressure drain valve controls the flow of low pressure condensed water to ensure condensed water and the sufficient exchange heat of pre-hot blast.(5) when Product Process needs to use low-pressure steam, high pressure heat exchanger, middle pressure heat exchanger and low pressure heat exchanger all use the low-pressure steam of outer confession, and the condensed water that high pressure heat exchanger, middle pressure heat exchanger and low pressure heat exchanger produce all enters condensate pump through low pressure drain valve.(6) when Product Process needs high steam, middle pressure heat exchanger and low pressure heat exchanger are without the need to using outer steam supply, the high pressure condensed water that high pressure heat exchanger produces and the middle pressure condensed water that middle pressure heat exchanger produces use without the need to relying on external user, namely loosening heat setting machine self achieves the cascade utilization of condensation water residual heat, avoids the discharge waste of condensation water residual heat.In like manner, when Product Process needs middle pressure steam, low pressure heat exchanger is without the need to using outer steam supply, the middle pressure condensed water that high pressure heat exchanger and middle pressure heat exchanger produce uses without the need to relying on external user, namely loosening heat setting machine self achieves making full use of of condensation water residual heat, avoids the discharge waste of condensation water residual heat.(7) when using high steam, new wind first through the air draft preheating that excess temperature is lower, then is heated by the low pressure heat exchanger that temperature is higher, presses heat exchanger heat, finally by the high pressure heat exchanger heating that temperature is the highest in then high by temperature; When using middle pressure steam, new wind, first through the air draft preheating that excess temperature is lower, is then heated by the low pressure heat exchanger that temperature is higher, presses heat exchanger and high pressure heat exchanger heating in then high by temperature; When using low-pressure steam, new wind, first through the air draft preheating that excess temperature is lower, is then heated by low pressure heat exchanger, middle pressure heat exchanger and high pressure heat exchanger that temperature is higher; In the process, the temperature of new wind improves step by step, and be also increase gradually to the temperature of the medium of its heating, the mode of this countercurrent flow totally maintains very high heat exchange efficiency.(8) the present invention is without the need to using flash tank, level pressure overflow valve and front pressure control valve, reduces cost, saves installing space, decrease floor space, avoids laxation shaping machine too bulky complex, is more conducive to arrange application in factory building.The pressure and temperature of saturated vapor and saturated condensed water is one to one, flash distillation utilizes waste heat just to reclaim difference between the sensible heat of condensed water under original pressure and the sensible heat under flashing pressure, and flashing pressure is lower, flash steam mobilization dynamic is lower, flash steam utilizes more difficult, therefore is difficult to condensed water to be reduced to less than 100 DEG C; Compared with reclaiming condensation water residual heat with flash distillation, middle pressure heat exchanger of the present invention reclaims high pressure condensed water sensible heat, low pressure heat exchanger presses condensed water sensible heat in reclaiming, and the exhaust temperature of condensed water can be reduced to less than 70 DEG C, and heat utilization rate is able to further raising.
As preferred version of the present invention, high-pressure steam pipe, middle pressure steam pipe are connected with main feed header with the 3rd stop valve respectively by the first stop valve, the second stop valve with low pressure steam pipe; Described main feed header is directly connected with the entrance of described high pressure heat exchanger, be connected with the entrance of described middle pressure heat exchanger by the 4th stop valve, be connected by the entrance of the 5th stop valve with described low pressure heat exchanger; Described first recycling condensing water pipe is provided with the 6th stop valve, and the outlet of described 6th stop valve is also connected with the entrance of described middle pressure heat exchanger; Described second recycling condensing water pipe is provided with the 7th stop valve, and the outlet of described 7th stop valve is also connected with the entrance of described low pressure heat exchanger; The outlet of described high pressure heat exchanger is provided with the 8th stop valve, and the rear of described 8th stop valve is in series with described high pressure drain valve; The outlet of described middle pressure heat exchanger is provided with the tenth stop valve, and the rear of described tenth stop valve is in series with described middle pressure drain valve; Between the entrance of described 8th stop valve and described tenth stop valve, cross-over connection has the 9th stop valve, and between described tenth stop valve and the entrance of described low pressure drain valve, cross-over connection has the 11 stop valve.(1) when Product Process needs to use high steam, open the first stop valve, the 6th stop valve, the 7th stop valve, the 8th stop valve and the tenth stop valve, close the second stop valve, the 3rd stop valve, the 4th stop valve, the 5th stop valve, the 9th stop valve and the 11 stop valve simultaneously; Now high pressure heat exchanger uses the high steam of outer confession, the condensed water of high pressure heat exchanger enters middle pressure heat exchanger through the 8th stop valve and high pressure drain valve, the condensed water of middle pressure heat exchanger enters low pressure heat exchanger through the tenth stop valve and middle pressure drain valve, and the condensed water that low pressure heat exchanger produces enters condensate pump through low pressure drain valve.(2) when Product Process needs to use middle pressure steam, open the second stop valve, 4th stop valve, 7th stop valve, 9th stop valve and the tenth stop valve, close the first stop valve simultaneously, 3rd stop valve, 5th stop valve, 6th stop valve, 8th stop valve and the 11 stop valve, now high pressure heat exchanger and middle pressure heat exchanger all use the middle pressure steam of outer confession, the condensed water that high pressure heat exchanger produces is through the 9th stop valve, tenth stop valve and middle pressure drain valve enter low pressure heat exchanger, the condensed water that middle pressure heat exchanger produces enters low pressure heat exchanger through the tenth stop valve and middle pressure drain valve, the condensed water that low pressure heat exchanger produces enters condensate pump through low pressure drain valve.(3) when Product Process needs to use low-pressure steam, open the 3rd stop valve, 4th stop valve, 5th stop valve, 9th stop valve and the 11 stop valve, close the first stop valve simultaneously, second stop valve, 6th stop valve, 7th stop valve, 8th stop valve and the tenth stop valve, now high pressure heat exchanger, middle pressure heat exchanger and low pressure heat exchanger all use the low-pressure steam of outer confession, the condensed water that high pressure heat exchanger produces is through the 9th stop valve, 11 stop valve and low pressure drain valve enter condensate pump, the condensed water that middle pressure heat exchanger produces enters condensate pump through the 11 stop valve and low pressure drain valve, the condensed water that low pressure heat exchanger produces directly enters condensate pump through low pressure drain valve.By the switching of valve, no matter Product Process needs high pressure or middle pressure steam, and heat exchanger is gross area use, drain valve all in design conditions work, and loosening heat setting machine self just can realize the cascade utilization of condensation water residual heat.
As preferred version of the present invention, the front and back of described high pressure drain valve, middle pressure drain valve and low pressure drain valve are in series with front stop valve and rear stop valve respectively, are parallel with bypass cutoff valve between the entrance of described front stop valve and the outlet of rear stop valve.Front stop valve and rear stop valve are normally in opening, when drain valve occurs that damage needs to change, close front stop valve and rear stop valve, open bypass cutoff valve, drain valve can be changed when not breaks in production, when heat exchanger uses condensed water heat exchange, also by regulating the aperture of front stop valve and rear stop valve to control flow.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation, and accompanying drawing only provides reference and explanation use, is not used to limit the present invention.
Fig. 1 is that without return air classification heat exchange, hydrophobic and air exhaust waste heat utilizes the schematic diagram of loosening heat setting machine in the present invention.
In figure: S1. high-pressure steam pipe; S2. middle pressure steam pipe; S3. low pressure steam pipe; S4. main feed header; E1. high pressure heat exchanger; E2. pressure heat exchanger in; E3. low pressure heat exchanger; E4. fresh air preheating device; W1. high pressure draining pipe; W2. pressure drain pipe in; W3. low pressure drain pipe; W4. the first recycling condensing water pipe; W5. the second recycling condensing water pipe; V1. the first stop valve; V2. the second stop valve; V3. the 3rd stop valve; V4. the 4th stop valve; V5. the 5th stop valve; V6. the 6th stop valve; V7. the 7th stop valve; V8. the 8th stop valve; V9. the 9th stop valve; V10. the tenth stop valve; V11. the 11 stop valve; Vt1. high pressure drain valve; Vt2. pressure drain valve in; Vt3. low pressure drain valve; P1. condensate pump; F1. new wind; F2. pre-hot blast; F4. hot blast; F6. air draft; Fy. blower fan.
Detailed description of the invention
As shown in Figure 1, without return air classification heat exchange, hydrophobic and air exhaust waste heat utilizes loosening heat setting machine in the present invention, the cabinets cavity of loosening heat setting machine is provided with blower fan Fy, drying chamber and heat exchanger, fresh air preheating device E4 is provided with outside casing, the inlet scoop of blower fan Fy communicates with the wind-supplying mouth on casing, and the air outlet of blower fan Fy aims at the heat exchanger of top, and the air outlet above heat exchanger enters drying chamber, be provided with exhaust outlet below drying chamber, exhaust outlet is led to outside casing by exhaust duct.
Discharge after exhaust duct access fresh air preheating device E4 makes air draft F6 and new wind F1 carry out indirect heat exchange.The below of fresh air preheating device E4 is provided with new wind entrance, and the top of fresh air preheating device E4 is provided with pre-hot-blast outlet, the wind-supplying mouth of pre-hot-blast outlet access loosening heat setting machine.
The air draft F6 of loosening heat setting machine accesses fresh air preheating device E4 and carries out preheating to new wind F1, and the waste heat in air draft F6 is recovered, and new wind F1 temperature is improved the wind-supplying mouth of rear feeding loosening heat setting machine.The pre-hot blast F2 entered from wind-supplying mouth enters the inlet scoop of blower fan Fy, and the wind that blower fan Fy blows out becomes hot blast F4 and enters drying chamber after heat exchanger heating, and the humid air in drying chamber is discharged by exhaust duct.
Heat exchanger comprises high pressure heat exchanger E1 stacked successively from top to bottom, middle pressure heat exchanger E2 and low pressure heat exchanger E3.Pre-hot blast is blown out by blower fan Fy, and when Product Process needs to use high steam, pre-hot blast first heats through the low pressure heat exchanger E3 that excess temperature is higher, presses heat exchanger E2 to heat, finally heated by the high pressure heat exchanger E1 that temperature is the highest in then high by temperature; When Product Process needs to use middle pressure steam, pre-hot blast first heats through the low pressure heat exchanger E3 that excess temperature is higher, presses heat exchanger E2 and high pressure heat exchanger E1 to heat in then high by temperature.In the process, the temperature of air improves step by step, is also increase gradually to the vapor (steam) temperature of its heating.
High-pressure steam pipe S1, middle pressure steam pipe S2 are connected with main feed header S4 with the 3rd stop valve V3 respectively by the first stop valve V1, the second stop valve V2 with low pressure steam pipe S3.Main feed header S4 is directly connected with the entrance of high pressure heat exchanger E1, be connected with the entrance of middle pressure heat exchanger E2 by the 4th stop valve V4, be connected with the entrance of low pressure heat exchanger E3 by the 5th stop valve V5.
The high pressure draining pipe W1 that high pressure heat exchanger E1 exports is in series with the 8th stop valve V8 and high pressure drain valve Vt1 successively, and the outlet of high pressure drain valve Vt1 is by pressing the entrance of heat exchanger E2 in the first recycling condensing water pipe W4 and the 6th stop valve V6 access.
The middle pressure drain pipe W2 that middle pressure heat exchanger E2 exports is in series with the tenth stop valve V10 and middle pressure drain valve Vt2 successively, and the outlet of middle pressure drain valve Vt2 accesses the entrance of low pressure heat exchanger E3 by the second recycling condensing water pipe W5 and the 7th stop valve V7.
The low pressure drain pipe W3 that low pressure heat exchanger E3 exports is provided with low pressure drain valve Vt3, the entrance of the outlet access condensate pump P1 of low pressure drain valve Vt3.Between the entrance of the 8th stop valve V8 and the tenth stop valve V10, cross-over connection has the 9th stop valve V9, and between the entrance of the tenth stop valve V10 and low pressure drain valve Vt3, cross-over connection has the 11 stop valve V11.
The front and back of high pressure drain valve Vt1, middle pressure drain valve Vt2 and low pressure drain valve Vt3 are in series with front stop valve and rear stop valve respectively, are parallel with bypass cutoff valve between the entrance of front stop valve and the outlet of rear stop valve.
When Product Process needs to use high steam, open the first stop valve V1, the 6th stop valve V6, the 7th stop valve V7, the 8th stop valve V8 and the tenth stop valve V10, close the second stop valve V2, the 3rd stop valve V3, the 4th stop valve V4, the 5th stop valve V5, the 9th stop valve V9 and the 11 stop valve V11 simultaneously; Now high pressure heat exchanger E1 uses the high steam of outer confession, and the high pressure condensed water that high pressure heat exchanger E1 produces is dredged out through the 8th stop valve V8 and high pressure drain valve Vt1, then enters middle pressure heat exchanger E2 through the first recycling condensing water pipe W4 and the 6th stop valve V6.In the flash distillation due to dilatation of middle pressure heat exchanger E2 mesohigh condensed water, condensed water pressure drop, flash steam and air heat-exchange be rapid condensation after discharging latent heat, non-flash distillation and the condensed water of the condensed water of pressure drop and time condensation presses condensed water in becoming continue to discharge sensible heat in middle pressure heat exchanger E2 after, middle pressure condensed water is dredged out through the tenth stop valve V10 and middle pressure drain valve Vt2, low pressure heat exchanger E3 is entered again through the second recycling condensing water pipe W5 and the 7th stop valve V7, middle pressure drain valve Vt2 presses the flow of condensed water to ensure condensed water and the sufficient exchange heat of pre-hot blast in controlling.In low pressure heat exchanger E3, the flash distillation again due to dilatation of middle pressure condensed water, condensed water pressure declines further, flash steam and air heat-exchange be rapid condensation after discharging latent heat, become low pressure condensed water after the condensed water of the condensed water that non-flash distillation and pressure decline further and three condensations continues to discharge sensible heat in low pressure heat exchanger E3 to dredge out from low pressure drain valve Vt3, low pressure drain valve Vt3 controls the flow of low pressure condensed water to ensure condensed water and the sufficient exchange heat of pre-hot blast.
When Product Process needs to use middle pressure steam, open the second stop valve V2, the 4th stop valve V4, the 7th stop valve V7, the 9th stop valve V9 and the tenth stop valve V10, close the first stop valve V1, the 3rd stop valve V3, the 5th stop valve V5, the 6th stop valve V6, the 8th stop valve V8 and the 11 stop valve V11, now high pressure heat exchanger E1 and middle pressure heat exchanger E2 all uses the middle pressure steam of outer confession simultaneously.The middle pressure condensed water that high pressure heat exchanger E1 produces is after the 9th stop valve V9 discharges, condensed water is pressed jointly to dredge out through the tenth stop valve V10 and middle pressure drain valve Vt2 in producing with middle pressure heat exchanger E2, middle pressure condensed water enters low pressure heat exchanger E3 through the second recycling condensing water pipe W5 and the 7th stop valve V7 again, in low pressure heat exchanger E3, the flash distillation due to dilatation of middle pressure condensed water, condensed water pressure drop, flash steam and air heat-exchange be rapid condensation after discharging latent heat, non-flash distillation and the condensed water of the condensed water of pressure drop and time condensation becomes low pressure condensed water continue to discharge sensible heat in low pressure heat exchanger E3 after dredge out from low pressure drain valve Vt3, low pressure drain valve Vt3 controls the flow of low pressure condensed water to ensure condensed water and the sufficient exchange heat of pre-hot blast.
When Product Process needs to use low-pressure steam, open the 3rd stop valve V3, the 4th stop valve V4, the 5th stop valve V5, the 9th stop valve V9 and the 11 stop valve V11, close the first stop valve V1, the second stop valve V2, the 6th stop valve V6, the 7th stop valve V7, the 8th stop valve V8 and the tenth stop valve V10, now high pressure heat exchanger E1, middle pressure heat exchanger E2 and low pressure heat exchanger E3 all use the low-pressure steam of outer confession simultaneously.The low pressure condensed water that high pressure heat exchanger E1 produces is dredged out through the 9th stop valve V9, the 11 stop valve V11 and low pressure drain valve Vt3, the low pressure condensed water that middle pressure heat exchanger E2 produces is dredged out through the 11 stop valve V11 and low pressure drain valve Vt3, and the low pressure condensed water that low pressure heat exchanger E3 produces directly is dredged out through low pressure drain valve Vt3.
The foregoing is only the better possible embodiments of the present invention, non-ly therefore limit to scope of patent protection of the present invention.In addition to the implementation, the present invention can also have other embodiments.All employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop in the protection domain of application claims.
Claims (2)
1. one kind without return air classification heat exchange, hydrophobic and air exhaust waste heat utilizes loosening heat setting machine, the cabinets cavity of loosening heat setting machine is provided with blower fan, heat exchanger and product is carried out to the drying chamber of shaping and drying, the inlet scoop of described blower fan communicates with the wind-supplying mouth on casing, the air outlet of blower fan aims at the heat exchanger of top, air outlet above described heat exchanger enters described drying chamber, exhaust outlet is provided with below drying chamber, described exhaust outlet leads to outside casing by exhaust duct, it is characterized in that: also comprise fresh air preheating device, the below of described fresh air preheating device is provided with new wind entrance, the top of fresh air preheating device is provided with pre-hot-blast outlet, the exhaust duct access fresh air preheating device of loosening heat setting machine makes air draft and new wind carry out indirect heat exchange, the described wind-supplying mouth of the pre-hot-blast outlet access loosening heat setting machine of described fresh air preheating device, described heat exchanger comprises high pressure heat exchanger stacked successively from top to bottom, middle pressure heat exchanger and low pressure heat exchanger, the entrance of described high pressure heat exchanger is connected with main feed header, the outlet access high pressure drain valve of described high pressure heat exchanger, the outlet of described high pressure drain valve accesses the entrance of described middle pressure heat exchanger by the first recycling condensing water pipe, drain valve is pressed in the outlet access of middle pressure heat exchanger, the outlet of middle pressure drain valve accesses the entrance of described low pressure heat exchanger by the second recycling condensing water pipe, low pressure heat exchanger exit is by low pressure drain valve access condensate pump, high-pressure steam pipe, middle pressure steam pipe are connected with main feed header with the 3rd stop valve respectively by the first stop valve, the second stop valve with low pressure steam pipe, described main feed header is directly connected with the entrance of described high pressure heat exchanger, be connected with the entrance of described middle pressure heat exchanger by the 4th stop valve, be connected by the entrance of the 5th stop valve with described low pressure heat exchanger, described first recycling condensing water pipe is provided with the 6th stop valve, and the outlet of described 6th stop valve is also connected with the entrance of described middle pressure heat exchanger, described second recycling condensing water pipe is provided with the 7th stop valve, and the outlet of described 7th stop valve is also connected with the entrance of described low pressure heat exchanger, the outlet of described high pressure heat exchanger is provided with the 8th stop valve, and the rear of described 8th stop valve is in series with described high pressure drain valve, the outlet of described middle pressure heat exchanger is provided with the tenth stop valve, and the rear of described tenth stop valve is in series with described middle pressure drain valve, between the entrance of described 8th stop valve and described tenth stop valve, cross-over connection has the 9th stop valve, and between described tenth stop valve and the entrance of described low pressure drain valve, cross-over connection has the 11 stop valve.
It is 2. according to claim 1 that without return air classification heat exchange, hydrophobic and air exhaust waste heat utilizes loosening heat setting machine, it is characterized in that: the front and back of described high pressure drain valve, middle pressure drain valve and low pressure drain valve are in series with front stop valve and rear stop valve respectively, are parallel with bypass cutoff valve between the entrance of described front stop valve and the outlet of rear stop valve.
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| CN201310025605.1A CN103088510B (en) | 2013-01-22 | 2013-01-22 | Non-return-air classification heat exchange dewatering and air exhaust waste heat utilization relaxation heat setting machine |
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| CN201310025605.1A CN103088510B (en) | 2013-01-22 | 2013-01-22 | Non-return-air classification heat exchange dewatering and air exhaust waste heat utilization relaxation heat setting machine |
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| CN201463489U (en) * | 2009-07-27 | 2010-05-12 | 上海是达环保节能设备有限公司 | Energy-saving device for heat pipe heat exchanger of baking oven |
| CN201731732U (en) * | 2010-07-09 | 2011-02-02 | 中钢集团洛阳耐火材料研究院有限公司 | Energy-saving fiber drying kiln |
| CN102878547A (en) * | 2012-10-17 | 2013-01-16 | 亿恒节能科技江苏有限公司 | Outer drying steam triple-effect heat exchange system |
| CN203096292U (en) * | 2013-01-22 | 2013-07-31 | 亿恒节能科技江苏有限公司 | Hierarchical heat exchanging water draining and discharged air waste heat utilization non-return-air relaxation heat setting machine |
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