CN104031793A - Energy-saving system for brewing white spirit by recycling steam and brewing method thereof - Google Patents

Energy-saving system for brewing white spirit by recycling steam and brewing method thereof Download PDF

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Publication number
CN104031793A
CN104031793A CN201410217729.4A CN201410217729A CN104031793A CN 104031793 A CN104031793 A CN 104031793A CN 201410217729 A CN201410217729 A CN 201410217729A CN 104031793 A CN104031793 A CN 104031793A
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China
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steam
pot
arm
gate valve
tube
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CN201410217729.4A
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Chinese (zh)
Inventor
邓运明
张成立
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Shanghai Jin Jiang River Electronic Technology Engineering Co Ltd
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Shanghai Jin Jiang River Electronic Technology Engineering Co Ltd
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Priority to CN201410217729.4A priority Critical patent/CN104031793A/en
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Abstract

The invention provides an energy-saving system for brewing white spirit by recycling steam. The energy-saving system comprises a steam supply device, a branch steam cylinder, a first pot, a second pot, a white spirit condenser, a compressor, a multi-stage condenser and an evaporator, wherein the branch steam cylinder is connected with the first pot and the second pot; an output pipe of the first pot is connected with a branch pipe A and a branch pipe B; an output pipe of the second pot is connected with a branch pipe C and a branch pipe D; a steam inlet of the white spirit condenser is connected with the branch pipe A and the branch pipe D; the inlet of the compressor is connected with the branch pipe B and the branch pipe C; the compressor is connected with the multi-stage condenser; the multi-stage condenser is connected with the evaporator; and the evaporator is connected with input pipes of the first pot and the second pot. By adopting the energy-saving system for brewing white spirit by recycling steam, the steam consumption cost can be reduced, and environmental pollution is reduced. The invention also provides a brewing method.

Description

A kind of brewing spirit energy conserving system and brewing method thereof of vapor recovery recycle
Technical field
The present invention relates to a kind of vapor recycling system, particularly relate to a kind of brewing spirit energy conserving system and brewing method thereof of vapor recovery recycle.
Background technology
China is the big country that produces white wine, white wine annual production 10 million ton, and producing white wine mean consumption quantity of steam per ton is 20 tons of left and right, consumption 3 tons of left and right of coal.Therefore produce every year white wine consumption steam, reach 200,000,000 tons, 3,000 ten thousand tons, consumption coal, its expense surpasses 20,000,000,000 Renminbi.
Conventionally in white wine manufacture craft, there is steaming grain acid discharge operation one, sour gas in grain and vinasse is steamed with convenient follow-up fermentation.This part consumes quantity of steam and accounts for 82% of total amount consumed, yet, current production white wine system can not be by the vapor recovery that contains sour gas the recycle of discharging from grain and vinasse, this steam that contains sour gas can only be directly discharged in environment, not only causes steam consumption cost high but also polluted environment.
Summary of the invention
The shortcoming of prior art in view of the above, first object of the present invention is to provide a kind of brewing spirit energy conserving system that can reduce steam consumption cost and reduce the vapor recovery recycle of environmental pollution.
Second object of the present invention is to provide a kind of brewing method of brewing spirit energy conserving system of vapor recovery recycle.
For realizing above-mentioned first object, the invention provides a kind of brewing spirit energy conserving system of vapor recovery recycle, at least comprise: for steam unit, with the described minute steam cylinder being connected for steam unit, first discriminates pot, and second discriminates pot, white wine condenser, compressor, multi-stage condensing device, and vaporizer;
Within described minute, steam cylinder is connected with the described first input tube of discriminating pot by being provided with the first steam output pipe of the first gate valve, and within described minute, steam cylinder is connected with the described second input tube of discriminating pot by being provided with the second steam output pipe of the second gate valve;
The described first output tube of discriminating pot is connected with the A arm that is provided with the 3rd gate valve and the B arm that is provided with the 4th gate valve;
The described second output tube of discriminating pot is connected with the C arm of the 5th gate valve and is provided with the 6th gate valve D arm;
The steam inlet of described white wine condenser is connected with D arm with described A arm;
The import of described compressor is connected with C arm with described B arm, and the outlet of described compressor is connected with the high-temperature steam import of described multi-stage condensing device;
Described multi-stage condensing device is connected with noncondensable gas storage tank, and the high-temperature water outlet of described multi-stage condensing device is connected with described evaporator by pipeline, and the condensation-water drain of described multi-stage condensing device connects water reservoir;
The outlet pipe of described vaporizer is connected with the E arm of the 7th gate valve and is provided with the F arm of the 8th gate valve, and the described E arm the other end is connected with the described first input tube of discriminating pot; The described F arm the other end is connected with the described second input tube of discriminating pot.
Further, described multi-stage condensing device comprises first-stage condenser and secondary condenser, the high-temperature steam import of described first-stage condenser is connected with the outlet of described compressor, the condensation-water drain of described first-stage condenser is connected with described secondary condenser import by pipeline, the high-temperature water outlet of described first-stage condenser is connected with described evaporator by pipeline, and the noncondensable gas outlet of described first-stage condenser is connected with described noncondensable gas storage tank by pipeline; The high-temperature water outlet of described secondary condenser is connected with the import of described first-stage condenser high-temperature water by pipeline; The condensation-water drain of described secondary condenser is connected with described water reservoir, and the entrance of cooling water of described secondary condenser is connected with apparatus for supplying cool water.
Further, described compressor is reciprocation compressor, radial compressor or Root's blower.
Further, the described first output tube of discriminating pot connects A Y-tube, and a side pipe of described A Y-tube is connected with the described first output tube of discriminating pot, and its another side pipe is connected with described B arm, and the supervisor of described A Y-tube is connected with described A arm.
Further, the described second output tube of discriminating pot connects B Y-tube, and a side pipe of described B Y-tube is connected with the described second output tube of discriminating pot, and its another side pipe is connected with described C arm, and the supervisor of described B Y-tube is connected with described D arm.
Further, the import of described compressor connects C Y-tube, and the supervisor of described C Y-tube is connected with the import of described compressor, and a side pipe of described C Y-tube is connected with described B arm, and its another side pipe is connected with described C arm.
Further, the outlet pipe of described vaporizer connects D Y-tube, and the supervisor of described D Y-tube is connected with the outlet pipe of described vaporizer, and a side pipe of described D Y-tube is connected with described E arm, and its another side pipe is connected with described F arm.
Further, described the first steam output pipe connects E Y-tube, a side pipe of described E Y-tube is connected with described the first steam output pipe, and its another side pipe is discriminated pot input aperture by pipeline and described first and is connected, and the supervisor of described E Y-tube is connected with described E arm.
Further, described the second steam output pipe connects F Y-tube, and a side pipe of described F Y-tube is connected with described the second steam output pipe, and its another side pipe and described second is discriminated pot input aperture and is connected, and the supervisor of described E Y-tube is connected with described F arm.
As mentioned above, the brewing spirit energy conserving system of a kind of vapor recovery recycle of the present invention, has following beneficial effect:
Because the C arm being connected with the described second output tube of discriminating pot is connected with described compressor inlet, the described B arm being connected with the described first output tube of discriminating pot is also connected with the import of described compressor, the outlet of described compressor and described multi-stage condensing device, described multi-stage condensing device is connected with noncondensable gas storage tank, the high-temperature water outlet of described multi-stage condensing device is connected with described evaporator by pipeline, and the condensation-water drain of described multi-stage condensing device connects water reservoir; And the outlet pipe of described vaporizer is connected with the described first input tube of discriminating pot by described E arm, the outlet pipe of described vaporizer is also connected with the described second input tube of discriminating pot by described F arm, thereby efficient recovery the used heat discharging in brewing spirit process, its circulation is re-used, not only reduce the consuming cost of steam, can also reduce environmental pollution.
For realizing above-mentioned second object, the invention provides a kind of brewing method of brewing spirit energy conserving system of above-mentioned vapor recovery recycle, comprise the steps:
1) pot is discriminated in preheating: open described the first gate valve and the second gate valve; The described steam unit that supplies was to described minute steam cylinder input steam, and within described minute, steam cylinder is given respectively the first described Zhen pot and the second Zhen pot input steam that grain and vinasse mixture are housed by the first described steam output pipe and the second steam output pipe;
2) steam wine: discriminate pot and second and discriminate and when the discharge of wine steam is arranged at pot top, cover pot cover when described first, turn described the first gate valve and the second gate valve down, close described the 4th gate valve, the 5th gate valve, the 7th gate valve and the 8th gate valve, open described the 3rd gate valve and the 6th gate valve, the wine steam that the first described Zhen pot and the second Zhen pot are discharged enters described white wine condenser; To the entrance of cooling water input water coolant of described white wine condenser, this water coolant finally flows out by the cooling water outlet of described white wine condenser simultaneously; Wine steam is cooled, and described white wine condenser flows out white wine phlegma;
3) steam grain: when white wine condensate stream is complete, close described the 3rd gate valve and the 6th gate valve, open described the 4th gate valve, the 5th gate valve, the 7th gate valve and the 8th gate valve, the high-temperature steam that the first described Zhen pot and the second Zhen pot are discharged enters described compressor and enters after compression described multi-stage condensing device, the high-temperature water that described multi-stage condensing device is discharged enters described vaporizer, and the high-temperature steam that described vaporizer is discharged enters described the first Zhen pot and second and discriminates pot; When steam flow reaches the flow of system needs in described E arm and F arm, close described the first gate valve and the second gate valve.
As mentioned above, the brewing method of the brewing spirit energy conserving system of vapor recovery recycle of the present invention, has following beneficial effect:
Used heat owing to discharging in can efficient recovery brewing spirit process, re-uses its circulation, thereby has not only reduced the consuming cost of steam, can also reduce environmental pollution.
Accompanying drawing explanation
Fig. 1 is shown as the schematic diagram of the brewing spirit energy conserving system of a kind of vapor recovery recycle of the present invention.
Element numbers explanation
1 for 2 minutes steam cylinders of steam unit
3 first discriminate pot 21 first steam output pipes
31 A arm 22 second steam output pipes
32 B arms 4 second are discriminated pot
5 white wine condenser 41 C arms
The entrance of cooling water 42 D arms of 51 white wine condensers
Cooling water outlet 6 compressors of 52 white wine condensers
7 vaporizer 81 noncondensable gas storage tanks
71 E arm 82 water reservoirs
72 F arm 91 first-stage condenser
101 first gate valve 92 secondary condensers
102 second gate valve 921 apparatus for supplying cool water
103 the 3rd gate valve 106 the 6th gate valves
104 the 4th gate valve 107 the 7th gate valves
105 the 5th gate valve 111 A Y-tubes
108 the 8th gate valve 112 B Y-tubes
113 C Y-tube 114 D Y-tubes
115 E Y-tube 116 F Y-tubes
Embodiment
By particular specific embodiment explanation embodiments of the present invention, person skilled in the art scholar can understand other advantages of the present invention and effect easily by the disclosed content of this specification sheets below.
Refer to Fig. 1.Notice, appended graphic the illustrated structure of this specification sheets, ratio, size etc., equal contents in order to coordinate specification sheets to disclose only, for person skilled in the art scholar, understand and read, not in order to limit the enforceable qualifications of the present invention, therefore the technical essential meaning of tool not, the adjustment of the modification of any structure, the change of proportionlity or size, do not affecting under the effect that the present invention can produce and the object that can reach, all should still drop in the scope that disclosed technology contents can contain.Simultaneously, in this specification sheets, quote as " on ", the term of D score, " left side ", " right side ", " centre " and " " etc., also only for ease of understanding of narrating, but not in order to limit the enforceable scope of the present invention, the change of its relativeness or adjustment, under without essence change technology contents, when being also considered as the enforceable category of the present invention.
As described in Figure 1, the invention provides a kind of brewing spirit energy conserving system of vapor recovery recycle, at least comprise: for steam unit 1, with the described minute steam cylinder 2 being connected for steam unit 1, first discriminates pot 3, the second discriminates pot 4, white wine condenser, compressor 6, multi-stage condensing device, and vaporizer 7.
Within described minute, steam cylinder 2 is connected with the described first input tube of discriminating pot 3 by being provided with the first steam output pipe 21 of the first gate valve 101, within described minute, steam cylinder 2 is connected with the described second input tube of discriminating pot 4 by being provided with the second steam output pipe 22 of the second gate valve 102, sees Fig. 1.
The described first output tube of discriminating pot 3 is connected with the A arm 31 that is provided with the 3rd gate valve 103 and the B arm 32 that is provided with the 4th gate valve 104; Preferably, the described first output tube of discriminating pot 3 connects A Y-tube 111, and a side pipe of described A Y-tube 111 is connected with the described first output tube of discriminating pot 3, and its another side pipe is connected with described B arm 32, the supervisor of described A Y-tube 111 is connected with described A arm 31, sees Fig. 1.
The described second output tube of discriminating pot 4 is connected with the C arm 41 of the 5th gate valve 105 and is provided with the D arm 42 of the 6th gate valve 106; Preferably, the described second output tube of discriminating pot 4 connects B Y-tube 112, and a side pipe of described B Y-tube 112 is connected with the described second output tube of discriminating pot 4, and its another side pipe is connected with described C arm 41, the supervisor of described B Y-tube 112 is connected with described D arm 42, sees Fig. 1.
The steam inlet of described white wine condenser is connected with D arm 42 with described A arm 31, sees Fig. 1.
The import of described compressor 6 is connected with C arm 41 with described B arm 32, preferably, the import of described compressor 6 connects C Y-tube 113, the supervisor of described C Y-tube 113 is connected with the import of described compressor 6, a side pipe of described C Y-tube 113 is connected with described B arm 32, and its another side pipe is connected with described C arm 41.The outlet of described compressor 6 is connected with the high-temperature steam import of described multi-stage condensing device; Preferably, described compressor 6 is reciprocation compressor 6, radial compressor 6 or Root's blower.Visible, first described high-temperature steams of discriminating pot the 3 and second Zhen pot 4 discharges can enter described compressor 6, and described compressor 6 can be compressed into high temperature and high pressure steam high-temperature steam and deliver in described multi-stage condensing device, sees Fig. 1.In addition, when multi-stage condensing device efficiency is very high, described compressor also can be changed with the position of described multi-stage condensing device.
With reference to figure 1, described multi-stage condensing device is connected with noncondensable gas storage tank 81, and the high-temperature water outlet of described multi-stage condensing device is connected with described vaporizer 7 imports by pipeline, and the condensation-water drain of described multi-stage condensing device connects water reservoir 82; Further, described multi-stage condensing device comprises first-stage condenser 91 and secondary condenser 92, the high-temperature steam import of described first-stage condenser 91 is connected with the outlet of described compressor 6, the condensation-water drain of described first-stage condenser 91 is connected with described secondary condenser 92 imports by pipeline, the high-temperature water outlet of described first-stage condenser 91 is connected with described vaporizer 7 imports by pipeline, and the noncondensable gas outlet of described first-stage condenser 91 is connected with described noncondensable gas storage tank 81 by pipeline; The high-temperature water outlet of described secondary condenser 92 is connected with the high-temperature water import of described first-stage condenser 91 by pipeline; The condensation-water drain of described secondary condenser 92 is connected with described water reservoir 82, and the entrance of cooling water of described secondary condenser 92 is connected with apparatus for supplying cool water 921.Visible, when described multi-stage condensing device absorbs the heat energy of the high temperature and high pressure steam of being sent into by described compressor 6 and obtains after high-temperature-hot-water, high-temperature-hot-water can flow into described vaporizer 7; For the ease of the abundant exchange of high temperature and high pressure steam heat energy, in high temperature and high pressure steam, non-condensable gas cognition enters described noncondensable gas storage tank 81.Preferably, described first-stage condenser 91 and secondary condenser 92 are heat tube type cold condenser, plate-type condenser, or plate-type heat exchanger.
With reference to figure 1, the outlet pipe of described vaporizer 7 is connected with the E arm 71 of the 7th gate valve 107 and is provided with the F arm 72 of the 8th gate valve 108; Preferably, the outlet pipe of described vaporizer 7 connects D Y-tube 114, and the supervisor of described D Y-tube 114 is connected with the outlet pipe of described vaporizer 7, and a side pipe of described D Y-tube 114 is connected with described E arm 71, and its another side pipe is connected with described F arm 72.Described E arm 71 the other ends are connected with the described first input tube of discriminating pot 3; Preferably, on described the first steam output pipe 21, connect E Y-tube 115, a side pipe of described E Y-tube 115 is connected with described the first steam output pipe 21, and its another side pipe is discriminated pot 3 input apertures by pipeline and described first and is connected, and the supervisor of described E Y-tube 115 is connected with described E arm 71.Described F arm 72 the other ends are connected with the described second input tube of discriminating pot 4; Preferably, on described the second steam output pipe 22, connect F Y-tube 116, a side pipe of described F Y-tube 116 is connected with described the second steam output pipe 22, and its another side pipe and described second is discriminated pot 4 input apertures and is connected, and the supervisor of described E Y-tube 115 is connected with described F arm 72.Visible, when the high-temperature-hot-water of being sent into by described multi-stage condensing device flashes to after high-temperature steam in described vaporizer 7, high-temperature steam can enter respectively the first described Zhen pot 3 and second by described E arm 71 and F arm 72 and discriminate in pot 4.
Hence one can see that, the high-temperature pressure steam giving off in brewing spirit process is compressed into the steam of High Temperature High Pressure through described compressor 6, the steam of High Temperature High Pressure is displaced high-temperature-hot-water after entering described multi-stage condensing device, high-temperature-hot-water flows into described vaporizer 7, described high-temperature-hot-water is flashed to high-temperature steam by described vaporizer 7, and high-temperature steam enters described first and discriminates pot the 3 and second Zhen pot 4; Thereby efficient recovery the used heat discharging in brewing spirit process, its circulation is re-used, not only reduced the consuming cost of steam, can also reduce environmental pollution.
In addition, described vaporizer 7 and described first-stage condenser 91 can be made of one, and the hydroecium of described first-stage condenser 91 can be worked as described vaporizer 7 uses simultaneously.
The present invention also provides a kind of brewing method of brewing spirit energy conserving system of vapor recovery recycle, comprises the steps:
1) pot is discriminated in preheating: open described the first gate valve 101 and the second gate valve 102; The described steam unit 1 that supplies was to described minute steam cylinder 2 input steam, and within described minute, steam cylinder 2 is given respectively first described Zhen the pot 3 and second Zhen pot 4 input steam that grain and vinasse mixture are housed by the first described steam output pipe 21 and the second steam output pipe 22; Along with constantly described first the discriminating pot 3 and second and discriminate pot 4 of input of steam, described first discriminates pot 3 and second discriminates grain in pot 4 and vinasse mixture by a fully preheating, sees Fig. 1.
2) steam wine: when first described Zhen pot 3 and second Zhen pot 4 tops have wine steam to discharge, cover pot cover, turn described the first gate valve 101 and the second gate valve 102 down, close described the 4th gate valve 104, the 5th gate valve 105, the 7th gate valve 107 and the 8th gate valve 108, open described the 3rd gate valve 103 and the 6th gate valve 106, make the first described wine steam of discriminating pot 3 discharges enter described white wine condenser by A arm 31, and the wine steam that the second described Zhen pot 4 is discharged enter described white wine condenser by D arm 42; To the entrance of cooling water 51 input water coolants of described white wine condenser, this water coolant finally flows out by the cooling water outlet 52 of described white wine condenser simultaneously; Wine steam is cooled, and now described white wine condenser flows out white wine phlegma, sees Fig. 1.
3) steam grain: when white wine condensate stream is complete, close described the 3rd gate valve 103 and the 6th gate valve 106, open described the 4th gate valve 104, the 5th gate valve 105, the 7th gate valve 107 and the 8th gate valve 108, at this moment the first described high-temperature steam of discriminating pot 3 discharges enters described compressor 6 by described B arm 32, the second described high-temperature steam of discriminating pot 4 discharges also enters described compressor 6 by described C arm 41, and described compressor 6 can be compressed into high temperature and high pressure steam high-temperature steam and deliver in described multi-stage condensing device; The high-temperature water that described multi-stage condensing device is discharged enters described vaporizer 7; Described vaporizer 7 flashes to high-temperature steam high-temperature water, and then high-temperature steam enters described the first Zhen pot 3 by described E arm 71, and enters described the second Zhen pot 4 by described F arm 72.When described E arm 71 and the interior steam flow of F arm 72 reach the flow that system needs, close described the first gate valve 101 and the second gate valve 102, see Fig. 1.
The used heat that adopts aforesaid method to discharge in can efficient recovery brewing spirit process in brewing spirit process, re-uses its circulation, thereby has not only reduced the consuming cost of steam, can also reduce environmental pollution.
In sum, brewing spirit energy conserving system and the brewing method thereof of a kind of vapor recovery recycle of the present invention, not only can reduce steam consumption cost, and can reduce environmental pollution.So the present invention has effectively overcome various shortcoming of the prior art and has had high industrial utilization.
Above-described embodiment is illustrative principle of the present invention and effect thereof only, but not for limiting the present invention.Any person skilled in the art scholar all can, under spirit of the present invention and category, modify or change above-described embodiment.Therefore, such as in affiliated technical field, have and conventionally know that the knowledgeable, not departing from all equivalence modifications that complete under disclosed spirit and technological thought or changing, must be contained by claim of the present invention.

Claims (10)

1. the brewing spirit energy conserving system of a vapor recovery recycle, it is characterized in that, at least comprise: for steam unit (1), with the described minute steam cylinder (2) being connected for steam unit (1), first discriminates pot (3), and second discriminates pot (4), white wine condenser (5), compressor (6), multi-stage condensing device, and vaporizer (7);
Described minute steam cylinder (2) by the first steam output pipe (21) that is provided with the first gate valve (101), be connected with the described first input aperture of discriminating pot (3), described minute steam cylinder (2) by being provided with second steam output pipe (22) of the second gate valve (102), be connected with the input aperture of described the second Zhen pot (4);
The described first output tube of discriminating pot (3) is connected with the B arm (32) that is provided with the A arm (31) of the 3rd gate valve (103) and is provided with the 4th gate valve (104);
The described second output tube of discriminating pot (4) is connected with the C arm (41) of the 5th gate valve (105) and is provided with the D arm (42) of the 6th gate valve (106);
The steam inlet of described white wine condenser (5) is connected with D arm (42) with described A arm (31);
The import of described compressor (6) is connected with C arm (41) with described B arm (32), and the outlet of described compressor (6) is connected with the high-temperature steam import of described multi-stage condensing device;
Described multi-stage condensing device is connected with noncondensable gas storage tank (81), and the high-temperature water outlet of described multi-stage condensing device is connected with described vaporizer (7) import by pipeline, and the condensation-water drain of described multi-stage condensing device connects water reservoir (82);
The outlet pipe of described vaporizer (7) is connected with the E arm (71) of the 7th gate valve (107) and is provided with the F arm (72) of the 8th gate valve (108), and described E arm (71) the other end is connected with the described first input aperture of discriminating pot (3); Described F arm (72) the other end is connected with the described second input aperture of discriminating pot (4).
2. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1, it is characterized in that: described multi-stage condensing device comprises first-stage condenser (91) and secondary condenser (92), the high-temperature steam import of described first-stage condenser (91) is connected with the outlet of described compressor (6), the condensation-water drain of described first-stage condenser (91) is connected with described secondary condenser (92) import by pipeline, the high-temperature water outlet of described first-stage condenser (91) is connected with described vaporizer (7) import by pipeline, the noncondensable gas outlet of described first-stage condenser (91) is connected with described noncondensable gas storage tank (81) by pipeline, the high-temperature water outlet of described secondary condenser (92) is connected with described first-stage condenser (91) high-temperature water import by pipeline, the condensation-water drain of described secondary condenser (92) is connected with described water reservoir (82), and the entrance of cooling water of described secondary condenser (92) is connected with apparatus for supplying cool water (921).
3. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1 and 2, is characterized in that: described compressor (6) is reciprocation compressor, radial compressor or Root's blower.
4. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1, it is characterized in that: the described first output tube of discriminating pot (3) connects A Y-tube (111), a side pipe of described A Y-tube (111) is connected with the described first output tube of discriminating pot (3), its another side pipe is connected with described B arm (32), and the supervisor of described A Y-tube (111) is connected with described A arm (31).
5. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1, it is characterized in that: the described second output tube of discriminating pot (4) connects B Y-tube (112), a side pipe of described B Y-tube (112) is connected with the described second output tube of discriminating pot (4), its another side pipe is connected with described C arm (41), and the supervisor of described B Y-tube (112) is connected with described D arm (42).
6. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1, it is characterized in that: the import of described compressor (6) connects C Y-tube (113), the supervisor of described C Y-tube (113) is connected with the import of described compressor (6), a side pipe of described C Y-tube (113) is connected with described B arm (32), and its another side pipe is connected with described C arm (41).
7. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1, it is characterized in that: the outlet pipe of described vaporizer (7) connects D Y-tube (114), the supervisor of described D Y-tube (114) is connected with the outlet pipe of described vaporizer (7), a side pipe of described D Y-tube (114) is connected with described E arm (71), and its another side pipe is connected with described F arm (72).
8. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1, it is characterized in that: described the first steam output pipe (21) connects E Y-tube (115), a side pipe of described E Y-tube (115) is connected with described the first steam output pipe (21), its another side pipe is discriminated pot (3) input aperture by pipeline and described first and is connected, and the supervisor of described E Y-tube (115) is connected with described E arm (71).
9. the brewing spirit energy conserving system of a kind of vapor recovery recycle according to claim 1, it is characterized in that: described the second steam output pipe (22) connects F Y-tube (116), a side pipe of described F Y-tube (116) is connected with the second steam output pipe (22), its another side pipe and described second is discriminated pot (4) input aperture and is connected, and the supervisor of described E Y-tube (115) is connected with described F arm (72).
10. the brewing method of the brewing spirit energy conserving system of a kind of vapor recovery recycle as claimed in claim 1, is characterized in that: comprise the steps:
1) pot is discriminated in preheating: open described the first gate valve (101) and the second gate valve (102); Described for steam unit (1) to described minute steam cylinder (2) input steam, described minute steam cylinder (2) by described the first steam output pipe (21) and the second steam output pipe (22), give respectively and be equipped with that described first of grain and vinasse mixture discriminated pot (3) and the second Zhen pot (4) is inputted a steam;
2) steam wine: discriminate pot (3) and second and discriminate and when the discharge of wine steam is arranged at pot (4) top, cover pot cover when described first, turn described the first gate valve (101) and the second gate valve (102) down, close described the 4th gate valve (104), the 5th gate valve (105), the 7th gate valve (107) and the 8th gate valve (108), open described the 3rd gate valve (103) and the 6th gate valve (106), the wine steam that the first described Zhen pot (3) and the second Zhen pot (4) are discharged enters described white wine condenser (5); To entrance of cooling water (51) the input water coolant of described white wine condenser, this water coolant finally flows out by the cooling water outlet (52) of described white wine condenser simultaneously; Wine steam is cooled, and described white wine condenser (5) flows out white wine phlegma;
3) steam grain: when white wine condensate stream is complete, close described the 3rd gate valve (103) and the 6th gate valve (106), open the 4th described gate valve (104), the 5th gate valve (105), the 7th gate valve (107) and the 8th gate valve (108), the high-temperature steam that the first described Zhen pot (3) and the second Zhen pot (4) are discharged enters described compressor (6) and enters after compression described multi-stage condensing device, the high-temperature water that described multi-stage condensing device is discharged enters described vaporizer (7), the high-temperature steam that described vaporizer (7) is discharged enters described the first Zhen pot (3) and second and discriminates pot (4), when steam flow reaches the flow of system needs in described E arm (71) and F arm (72), close described the first gate valve (101) and the second gate valve (102).
CN201410217729.4A 2014-05-20 2014-05-20 Energy-saving system for brewing white spirit by recycling steam and brewing method thereof Pending CN104031793A (en)

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104560582A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Energy-saving cooking system used for liquor vapor recovery and cyclic utilization and cooking method
CN104560515A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Steamer pot with rotary seal lifting structure and white spirit making energy-saving system
CN104560583A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Energy-saving steaming system capable of recycling steam and steaming method
CN104560584A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Energy-saving tube nest heat exchanger for steaming grains and energy-saving white spirit brewing system
CN104564672A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Roots compressor and oil filling and discharging method thereof as well as white spirit brewing energy-saving system
CN107338158A (en) * 2017-08-22 2017-11-10 泸州老窖集团有限责任公司 Steam grain device and steam grain method
CN108106051A (en) * 2017-07-10 2018-06-01 昊姆(上海)节能科技有限公司 For the energy-saving environmental protection device between brewing
CN113652331A (en) * 2021-08-17 2021-11-16 张桓川 Multifunctional steam-circulating liquor making system
CN113652331B (en) * 2021-08-17 2024-04-19 张桓川 System is made to multi-functional steam cycle's white spirit

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JPH04366301A (en) * 1991-06-13 1992-12-18 Hisaka Works Ltd Pure steam generator for food
CN203159585U (en) * 2013-01-30 2013-08-28 赵文志 Novel clean brewing steamer
CN103657124A (en) * 2012-09-20 2014-03-26 山西鼎圣精工有限公司 Alcohol distilling device
CN103706141A (en) * 2014-01-22 2014-04-09 象山医疗精密仪器有限公司 Steam compressed type alcohol recycling tower and distillation method

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JPH04366301A (en) * 1991-06-13 1992-12-18 Hisaka Works Ltd Pure steam generator for food
CN103657124A (en) * 2012-09-20 2014-03-26 山西鼎圣精工有限公司 Alcohol distilling device
CN203159585U (en) * 2013-01-30 2013-08-28 赵文志 Novel clean brewing steamer
CN103706141A (en) * 2014-01-22 2014-04-09 象山医疗精密仪器有限公司 Steam compressed type alcohol recycling tower and distillation method

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104560582A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Energy-saving cooking system used for liquor vapor recovery and cyclic utilization and cooking method
CN104560515A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Steamer pot with rotary seal lifting structure and white spirit making energy-saving system
CN104560583A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Energy-saving steaming system capable of recycling steam and steaming method
CN104560584A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Energy-saving tube nest heat exchanger for steaming grains and energy-saving white spirit brewing system
CN104564672A (en) * 2014-12-31 2015-04-29 上海锦江电子技术工程有限公司 Roots compressor and oil filling and discharging method thereof as well as white spirit brewing energy-saving system
CN104564672B (en) * 2014-12-31 2019-03-26 上海锦江电子技术工程有限公司 A kind of lobed rotor compressor, its oiling are drained the oil method and brewing spirit energy conserving system
CN108106051A (en) * 2017-07-10 2018-06-01 昊姆(上海)节能科技有限公司 For the energy-saving environmental protection device between brewing
CN107338158A (en) * 2017-08-22 2017-11-10 泸州老窖集团有限责任公司 Steam grain device and steam grain method
CN113652331A (en) * 2021-08-17 2021-11-16 张桓川 Multifunctional steam-circulating liquor making system
CN113652331B (en) * 2021-08-17 2024-04-19 张桓川 System is made to multi-functional steam cycle's white spirit

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