WO2018232825A1 - 自动化冲洗酒瓶回收装置 - Google Patents

自动化冲洗酒瓶回收装置 Download PDF

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Publication number
WO2018232825A1
WO2018232825A1 PCT/CN2017/094381 CN2017094381W WO2018232825A1 WO 2018232825 A1 WO2018232825 A1 WO 2018232825A1 CN 2017094381 W CN2017094381 W CN 2017094381W WO 2018232825 A1 WO2018232825 A1 WO 2018232825A1
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WO
WIPO (PCT)
Prior art keywords
tank
pipe
storage tank
disposed
citric acid
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Application number
PCT/CN2017/094381
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English (en)
French (fr)
Inventor
郑祥兵
郑剑峰
Original Assignee
盐城市剑峰机械有限公司
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Application filed by 盐城市剑峰机械有限公司 filed Critical 盐城市剑峰机械有限公司
Publication of WO2018232825A1 publication Critical patent/WO2018232825A1/zh

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto 
    • B08B9/08—Cleaning containers, e.g. tanks
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto 
    • B08B9/08—Cleaning containers, e.g. tanks
    • B08B9/0856—Cleaning of water-treatment installations
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material

Definitions

  • the invention relates to a wine bottle cleaning device, in particular to an automatic washing wine bottle recycling device.
  • the cleaning liquid is generally prepared by water and acid at a certain temperature. At present, the water is added to the barrel by a certain proportion, and the acid is added to the barrel. The water-acid mixture liquid is heated to form a cleaning liquid, which has high labor intensity, long preparation time, low automation degree, and inaccurate temperature control. The prepared cleaning liquid is difficult to reach the standard, and the cleaning effect is poor, and the cleaning liquid is cleaned after the bottle is cleaned. Directly discharged, it is easy to cause acid emissions pollution and water waste, and can not respond to the national call for energy conservation and emission reduction.
  • the technical problem to be solved by the present invention is to provide an automated washing bottle recycling device with high degree of automation.
  • an automatic washing wine bottle recycling device including: a steam heater, a citric acid tank, a mixing tank, a washing liquid tank, a washing host, a mixing a citric acid backwater storage tank, a strainer, a precision filter and an intermediate storage tank, wherein a steam heating pipe is disposed in the steam heater, and a steam heating pipe is connected to an upper end of the steam heater a steam inlet main pipe, wherein a steam pneumatic diaphragm regulating valve is disposed on the steam inlet main pipe, and a first steam main stop valve and a second are respectively disposed on the steam inlet main pipes on both sides of the steam pneumatic diaphragm regulating valve a steam shut-off valve, a steam filter is disposed on a steam inlet main pipe between the first steam shutoff valve and the steam pneumatic diaphragm regulating valve, and a steam heating pipe is connected to a lower end of the steam heater a condens
  • the mixing tank return pipe is provided with a mixing tank return pump, and the lower end of the other side of the mixing tank is provided with a temperature measuring device and an electric heat conducting instrument, and the temperature measuring device passes through the first wire and the steam pneumatic membrane regulating valve phase Connection
  • the electric heat conduction meter is connected to the citric acid centrifugal pump through a second wire, and the lower end of the mixing tank communicates with the upper end of the cleaning liquid storage tank through the mixing tank outlet pipe, and the mixing tank is arranged on the dispensing tank outlet pipe
  • the liquid discharging pump is provided with a mixing tank shut-off valve and a mixing tank filter on the mixing tank outlet pipe between the mixing tank discharging pump and the mixing tank, and the dispensing tank discharging pump and the cleaning liquid storage tank are arranged
  • the mixing tank discharge pipe is provided with a compounding liquid electromagnetic valve, and the mixing tank discharging pump is connected with the upper and lower limit alarm devices of the mixing tank magnetic flap level meter through the third wire, in the cleaning liquid storage tank a cleaning
  • a cleaning liquid storage tank filter wherein the lower end of the cleaning main body communicates with the upper end of the mixed citric acid return water temporary storage tank through the cleaning main body outlet pipe, and the mixed lemon is disposed at the lower end of the mixed citric acid return water temporary storage tank
  • An acid return water temporary storage tank sewage pipe, and a mixed citric acid return water temporary storage tank sewage discharge valve is arranged on the mixed citric acid return water temporary storage tank sewage pipe, on one side of the mixed citric acid return water temporary storage tank
  • the upper end is provided with a float control device, and the mixed citric acid is returned to the water.
  • the lower end of the storage tank is connected to the coarse filter through the mixed citric acid return water temporary storage tank outlet pipe, and the coarse filter is connected to the precision filter through the coarse filter outlet pipe, and the raw filter is arranged on the outlet pipe of the coarse filter a coarse filter liquid return pump, wherein the coarse filter liquid return pump is connected to the float control device through a fifth wire, and a coarse filter cutoff is arranged on the coarse filter discharge pipe between the coarse filter liquid return pump and the coarse filter a valve and a strainer filter, a first pressure gauge is disposed on the strainer outlet pipe between the strainer return pump and the precision filter, and the precision filter passes through the precision filter outlet pipe and the intermediate storage
  • the upper ends of the tanks communicate with each other, and a second pressure gauge is disposed on one end of the precision filter outlet pipe near the precision filter, and the cleaning fluid tank overflow port passes through the cleaning fluid tank overflow pipe and the second pressure a precision filter outlet pipe between the watch and the intermediate storage tank is in communication with each other, and a cleaning fluid storage tank overflow pump
  • a steam intake auxiliary pipe communicating with the steam inlet main pipe is disposed in parallel, and the steam inlet and exhaust pipe is disposed on the steam inlet pipe
  • a steam sub-shutoff valve, the steam pneumatic diaphragm regulating valve, the first steam main shut-off valve, the second steam shut-off valve and the steam filter are located on the steam inlet main pipe between the two ends of the steam intake auxiliary pipe.
  • a condensed water outlet sub-pipe connected to the condensed water outlet main pipe is arranged in parallel, and the condensed water outlet sub-tube is provided with A condensed water secondary shutoff valve, the condensate trap, the first condensate shutoff valve, the second condensate shutoff valve, and the condensate filter are located on the condensate outlet main between the two ends of the condensate outlet subpipe.
  • the invention has the advantages that: the above-mentioned automatic washing wine bottle recycling device can automatically add water and acid, realize the heating while adding water, and control the temperature of the water at any time through the temperature measuring device, and control the proportion of acid at any time through the heat conducting instrument, thereby reducing the ratio of the acid.
  • the labor intensity of the workers is short, the speed is fast, the degree of automation is high, the temperature control is accurate, the prepared cleaning liquid can always reach the use standard, the cleaning effect is good, and the cleaning liquid can be recycled and filtered after cleaning the bottle. It will not cause acid emission pollution and waste of water resources, and can respond to the call for national energy conservation and emission reduction.
  • the auxiliary pipe can be used to continue the intake and outlet water without delay. Run, work efficiently.
  • FIG. 1 is a schematic view showing the structure of an automatic washing wine bottle recycling device of the present invention.
  • the automatic washing wine bottle recovery device comprises: steam heater 1, citric acid tank 2, mixing tank 3, cleaning liquid storage tank 4, cleaning main machine 5, mixed citric acid return water temporary storage tank 6, coarse A filter 7, a precision filter 8 and an intermediate storage tank 9 are provided with a steam heating pipe 10 in the steam heater 1, and a steam communicating with the steam heating pipe 10 is provided at one end of the steam heater 1
  • An intake main pipe 11 is provided with a steam pneumatic diaphragm regulating valve 12 on the steam inlet main pipe 11, and a first steam main stop valve is respectively disposed on the steam inlet main pipe 11 on both sides of the steam pneumatic diaphragm regulating valve 12 13 and a second steam shutoff valve 14, a steam filter 15 is disposed on the steam inlet main pipe 11 between the first steam shutoff valve 13 and the vapor pneumatic diaphragm regulating valve 12, and one of the steam heaters 1
  • the lower end of the side is provided with a condensate water discharge main pipe 16 communicating with the steam heating pipe 10, and a condensed water trap
  • a citric acid inlet pipe 26 is disposed at an upper end of the citric acid tank 2
  • a citric acid tank sewage pipe 27 is disposed at a lower end of the citric acid tank 2, and is disposed on the citric acid tank sewage pipe 27.
  • citric acid tank drain valve 271 There is a citric acid tank drain valve 271, and a citric acid tank magnetic flap level gauge upper and lower limit alarm device 272 is disposed on one side of the citric acid tank 2, and the lower end of the citric acid tank 2 passes through the citric acid outlet pipe 28
  • the citric acid outlet pipe 28 is provided with a citric acid centrifugal pump 29, and the citric acid discharge pipe 28 between the citric acid centrifugal pump 29 and the citric acid tank 2 is disposed on the citric acid outlet pipe 28.
  • the citric acid tank shut-off valve 30 and the citric acid tank filter 31 are provided with a stirring motor 32 at the upper end of the mixing tank 3, and the motor shaft of the stirring motor 32 extends into the mixing tank 3 and is connected to the stirring shaft 33.
  • a plurality of agitating blades 34 are disposed on the agitating shaft 33, and a mixing tank drain pipe 35 is disposed at a lower end of the mixing tank 3, and a mixing tank drain valve 36 is disposed on the mixing tank drain pipe 35.
  • One side of the tank 3 is provided with a tank magnetic flap level gauge upper and lower limit alarm device 37, The other side of the other side of the mixing tank 3 is provided with a tank overflow port 38, and the position of the tank overflow 38 is higher than the upper limit of the upper and lower limit alarm devices 37 of the tank magnetic level gauge.
  • the overflow port 38 communicates with the inlet pipe 21 between the inlet water solenoid valve 22 and the steam heater 1 through the mixing tank return pipe 39, and the mixing tank return pipe 39 is provided with a compound tank return pump 40,
  • the lower end of the other side of the mixing tank 3 is provided with a temperature measuring device 41 and an electric heat conductivity meter 42.
  • the temperature measuring device 41 is connected to the vapor pneumatic membrane regulating valve 12 through a first wire 43, and the electric heat conducting device 42 passes through the second
  • the wire 44 is connected to the citric acid centrifugal pump 29, and the lower end of the mixing tank 3 communicates with the upper end of the cleaning liquid storage tank 4 through the mixing tank outlet pipe 45, and the mixing tank is provided on the dispensing tank outlet pipe 45.
  • a compound tank shut-off valve 47 and a compound tank filter 48 are disposed on the mixing tank outlet pipe 45 between the tank discharge pump 46 and the cleaning fluid tank 4, and a compounding liquid solenoid valve 49 is disposed.
  • the dispensing tank discharge pump 46 is connected to the mixing tank magnetic flap level gauge upper and lower limit alarm device 37 through the third wire 50, and the cleaning liquid tank drain pipe 51 is disposed at the lower end of the cleaning liquid storage tank 4,
  • the cleaning liquid storage tank sewage pipe 51 is provided with a cleaning liquid storage tank sewage valve 52, and a cleaning liquid storage tank magnetic flap liquid level gauge upper and lower limit alarm device 53 is disposed on one side of the cleaning liquid storage tank 4,
  • the cleaning liquid storage tank magnetic flap level gauge upper and lower limit alarm device 53 is connected to the mixing tank discharge pump 46 through the fourth wire 54, and the cleaning liquid storage tank overflow is arranged at the upper end of the other side of the cleaning liquid storage tank 4.
  • the flow port 55, the position of the cleaning liquid storage tank overflow port 55 is higher than the upper limit position of the cleaning liquid storage tank magnetic flap level upper and lower limit alarm device 53, at the lower end of the other side of the cleaning liquid storage tank 4
  • a sampling tube 56 is disposed, and a sampling ball valve 57 is disposed on the sampling tube 56, and the lower end of the cleaning liquid storage tank 4 passes
  • the washing liquid tank outlet pipe 58 communicates with one side of the washing main body 5, and the cleaning liquid storage tank outlet pipe 58 is provided with a cleaning liquid storage tank discharge pump 59, and the cleaning liquid storage tank is discharged
  • the cleaning liquid storage tank outlet pipe 58 between the pump 59 and the cleaning liquid storage tank 4 is provided with a cleaning liquid storage tank shut-off valve 60 and a cleaning liquid storage tank filter 61, and the lower end of the cleaning main body 5 is discharged through the cleaning main body.
  • the tube 62 is in communication with the upper end of the mixed citric acid backwater storage tank 6, and a mixed citric acid backwater storage tank drain pipe 63 is disposed at the lower end of the mixed citric acid return water temporary storage tank 6, in which the mixed lemon is
  • the acid return water temporary storage tank sewage pipe 63 is provided with a mixed citric acid return water temporary storage tank sewage valve 64, and a floating ball control device 65 is disposed at an upper end of the mixed citric acid return water temporary storage tank 6
  • the lower end of the mixed citric acid backwater storage tank 6 is in communication with the strainer 7 by mixing the citric acid return water temporary storage tank outlet pipe 66, and the coarse filter 7 is passed through the coarse filter.
  • the liquid outlet pipe 67 and the precision filter 8 are in communication with each other, and a coarse filter liquid return pump 68 is disposed on the coarse filter liquid discharge pipe 67, and the coarse filter liquid return pump 68 passes through the fifth wire 69 and the float control device.
  • a strainer shut-off valve 70 and a strainer filter 71 are disposed on the strainer outlet pipe 67 between the coarse filter return pump 68 and the strainer 7, at which the back filter pump 68 is
  • a first pressure gauge 72 is disposed on the coarse filter outlet pipe 67 between the precision filter 8, and the precision filter 8 communicates with the upper end of the intermediate storage tank 9 through the precision filter outlet pipe 73.
  • a second pressure gauge 76 is disposed on one end of the precision filter outlet pipe 73 adjacent to the precision filter 8, and the cleaning fluid reservoir overflow port 55 passes through the cleaning fluid storage tank overflow pipe 77 and the second pressure gauge 76 and the middle
  • the fine filter discharge pipes 73 between the storage tanks 9 are in communication with each other, and a cleaning liquid storage tank overflow pump 78 is disposed on the cleaning liquid storage tank overflow pipe 77, and a lower end of the intermediate storage tank 9 is provided with An intermediate tank drain pipe 79 is disposed on the intermediate tank drain pipe 79 with an intermediate tank drain valve 80, in the middle
  • One side of the storage tank 9 is provided with an intermediate storage tank magnetic flap level gauge upper and lower limit alarm device 81, and the intermediate storage tank flap level gauge upper and lower limit alarm device 81 passes through the sixth conductor 82 and the strainer return pump 68 is connected, and the lower end of the intermediate storage tank 9 communicates with the inlet pipe 21 between the inlet water solenoid valve 22 and the steam heater 1 through the intermediate storage tank discharge pipe 83
  • a steam intake auxiliary pipe 89 communicating with each other is disposed in parallel with the steam intake main pipe 11, and a steam sub-stop valve is disposed on the steam intake auxiliary pipe 89. 90.
  • the steam pneumatic membrane regulating valve 12, the first steam main shutoff valve 13, the second steam shutoff valve 14 and the steam filter 15 are located on the steam inlet main pipe 11 between the both ends of the steam inlet sub-pipe 89.
  • a condensed water outlet sub-pipe 91 communicating with the condensed water discharge main pipe 16 is disposed in parallel, and a condensed water sub-cut is provided on the condensed water discharge sub-tube 91.
  • the valve 92, the condensate trap 16, the first condensate shutoff valve 18, the second condensate shutoff valve 19, and the condensate filter 20 are located on the condensate outlet main 16 between the ends of the condensate outlet sub-pipe 91. .
  • the steam pneumatic pneumatic regulating valve 12, the first steam main shut-off valve 13, the second steam main shut-off valve 14 and the water inlet electromagnetic on the inlet pipe 21 of the steam inlet main pipe 11 are simultaneously opened.
  • the valve 22 water enters the steam heater 1 from the inlet pipe 21, and the steam enters the steam heating pipe 10 in the steam heater 1 from the steam inlet main pipe 11, and the steam filter 15 filters the steam, and the steam transfers the heat.
  • the water flowing through the steam heating pipe 10 is transferred to the steam heater 1 to be heated, and the condensed water generated after the steam heating can be opened by opening the condensed water trap 17, the first condensed water shutoff valve 18, and the second condensed water shutoff valve 19
  • the condensed water outlet main pipe 16 is discharged, and the condensed water filter 20 can filter the condensed water.
  • the heated water in the steam heater 1 enters the mixing tank 3 through the outlet pipe 23, and opens the citric acid centrifugal pump 29 and the lemon.
  • the temperature measuring device 41 transmits a temperature signal to the control device, and the control device controls the steam-pneumatic membrane regulating valve 12 through the first wire 43 to provide a larger
  • the steam of the flow rate causes the water passing through the steam heater 1 to be heated.
  • the temperature measuring device 41 transmits a temperature signal to the control device, and the control device controls the steam pneumatic diaphragm regulating valve through the first wire 43.
  • the electrical conductivity meter 42 detects the acidity of the aqueous acid mixture in the mixing tank 3 at any time, and when the acidity is too low, the electrical conductivity meter 42 will signal It is transmitted to the control device, and the control device controls the citric acid centrifugal pump 29 to open through the second wire 44, and the citric acid continues to enter the mixing tank 3.
  • the electrical conductivity meter 42 transmits the signal to the control device, and the control device
  • the signal is controlled by the second wire 44 to control the citric acid centrifugal pump 29 to be closed, the citric acid stops entering the mixing tank 3; the stirring motor 32 is activated, and the motor shaft of the stirring motor 32 drives the stirring shaft 33.
  • the stirring shaft 33 drives the stirring blade 34 to rotate and mix and mix the mixing liquid in the mixing tank 3, and when the liquid level in the mixing tank 3 reaches the lower limit of the upper and lower limit alarm device 37 of the mixing tank magnetic flap level gauge, the mixing is performed.
  • the tank magnetic flap level gauge upper and lower limit alarm device 37 alarms and transmits the signal to the control device, and the control device controls the dispensing tank discharge pump 46 to be closed by the third wire 50, and the cleaning liquid in the tank 3 is stopped and enters the cleaning liquid storage tank. 4, when the liquid level in the mixing tank 3 reaches the upper limit position of the upper and lower limit alarm device 37 of the tank magnetic flap level meter, the tank magnetic flap level gauge upper and lower limit alarm device 37 is adjusted and the signal is transmitted to the control.
  • the device controls the adjusting tank discharge pump 46 to open through the third wire 50, and the cleaning liquid in the mixing tank 3 continues to enter the cleaning liquid storage tank 4, when the mixed liquid in the mixing tank 3 exceeds the level of the magnetic flap of the mixing tank
  • the mixing tank return pump 40 is started to re-feed the mixed liquid overflowed from the tank overflow port 38 to the inlet pipe 21 for recirculation, and the overflowed mixture can be re-entered with the water into the mixing tank 3, when the tank is adjusted.
  • the mixing tank shut-off valve 47 and the compounding liquid electromagnetic valve 49 are simultaneously opened, and the prepared cleaning liquid in the mixing tank 3 is introduced into the cleaning liquid storage tank 4 through the mixing tank outlet pipe 45, and the tank filter is adjusted.
  • the device 48 can filter the cleaning liquid in the dispensing tank outlet pipe 45; the sampling ball valve 57 is opened, and the cleaning liquid in the cleaning liquid storage tank 4 can be taken out through the sampling tube 56 for detection, when in the cleaning liquid storage tank 4
  • the cleaning liquid reaches the lower limit position of the upper and lower limit alarm device 53 of the magnetic liquid level gauge of the cleaning liquid storage tank, the upper and lower limit alarm device 53 of the magnetic liquid leveling device of the cleaning liquid storage tank alarms and transmits the signal to the control device, and the control device can
  • the mixing tank discharge pump 46 is controlled to be opened by the fourth wire 54, and the cleaning liquid in the mixing tank 3 continues to enter the cleaning liquid storage tank 4, when the cleaning liquid in the cleaning liquid storage tank 4 reaches the magnetic liquid level of the cleaning liquid storage tank Counting the upper limit
  • the cleaning liquid stops entering the cleaning liquid storage tank 4, when the cleaning liquid in the cleaning liquid storage tank 4 exceeds the upper limit of the upper and lower limit alarm device 53 of the cleaning liquid storage tank magnetic flap level level gauge and overflows from the cleaning liquid storage tank
  • the cleaning liquid storage tank overflow pump 78 is started, and the cleaning liquid overflowing from the cleaning liquid storage tank overflow port 55 is sent to the middle through the cleaning liquid storage tank overflow pipe 77 and the fine filter discharge pipe 73.
  • the cleaning liquid storage tank shut-off valve 60 is simultaneously opened, and the cleaning liquid in the cleaning liquid storage tank 4 is sent to the cleaning main body 5 to clean the wine bottle.
  • the washed mixed citric acid water enters the mixed citric acid backwater storage tank 6 by washing the main body outlet pipe 62, when mixed
  • the signal is transmitted to the control device through the float control device 65, and the control device controls the coarse filter return pump 68 to be opened by the fifth wire 69.
  • the coarse filter shut-off valve 70 is opened, and the mixed citric acid water in the mixed citric acid backwater storage tank 6 is sequentially passed through the citric acid return water temporary storage tank outlet pipe 66, the coarse filter 7, the coarse filter outlet pipe 67, and the precision filtration.
  • the filter 8 and the precision filter outlet pipe 73 reach the intermediate storage tank 9, the coarse filter 7 performs large particle filtration on the mixed citric acid water, and the coarse filter filter 71 can re-filter the mixed liquid passing through the coarse filter outlet pipe 67.
  • the precision filter 8 can precisely filter the mixed liquid after two filtrations, and the cleaning liquid after three times of filtration enters the intermediate storage tank 9; when the cleaning liquid in the intermediate storage tank 9 reaches the intermediate storage tank magnetic turnover liquid
  • the intermediate storage tank flipper level gauge upper and lower limit alarm device 81 transmits a signal to the control device, and the control device controls the coarse filter return pump 68 to be opened by the sixth wire 82, among which
  • the intermediate storage magnetic flap level gauge upper and lower limit alarm device 81 transmits a signal to the control device, and the control device
  • the intermediate storage tank return pump 84 is controlled
  • the cleaning liquid in the intermediate storage tank 9 passes directly through the intermediate storage tank.
  • the outlet pipe 83 is re-supplied into the inlet pipe 21 for recirculation to be re-entered into the mixing tank 3 together with the water.
  • the impurities precipitated in the cleaning liquid storage tank 4 can be discharged through the cleaning liquid storage tank sewage pipe 51, and the mixed citric acid return water temporary storage tank sewage valve 64 is opened to mix the impurities precipitated in the mixed citric acid return water temporary storage tank 6 by mixing the lemon.
  • the acid return water temporary tank drain pipe 63 is discharged, and the intermediate tank drain valve 80 is opened to discharge the impurities deposited in the intermediate tank 9 through the intermediate tank drain pipe 79.
  • the first steam main shutoff valve 13 and the second steam main shutoff valve 14 on the steam inlet main pipe 11 are simultaneously closed, and the steam intake auxiliary pipe 89 is opened.
  • the steam secondary shut-off valve 90 the steam can continue to enter the steam heating pipe 10 in the steam heater 1 from the steam intake auxiliary pipe 89, and the normal operation of the equipment can be ensured while repairing and replacing the steam pneumatic diaphragm regulating valve 12.
  • the above-mentioned automatic flushing wine bottle recovery device inspects the condensed water trap 17 , the first condensed water shutoff valve 18 and the second condensed water shutoff valve 19 are closed at the same time, and the condensed water secondary shutoff valve 92 on the condensed water outlet auxiliary pipe 91 is opened.
  • the condensed water can be discharged from the condensate water outlet pipe 91, and the normal operation of the equipment can be ensured while repairing and replacing the condensate trap 17 .
  • the above-mentioned automatic washing wine bottle recycling device can automatically add water and add acid, realize the heating while adding water, and control the temperature of the water at any time through the temperature measuring device, and control the proportion of acid at any time through the heat conducting instrument, thereby reducing the labor intensity of the worker and blending
  • the time is short, the speed is fast, the degree of automation is high, the temperature control is precise, the prepared cleaning liquid can always reach the use standard, the cleaning effect is good, and the cleaning liquid enters the bottle After cleaning, it can be recycled and reused, which will not cause acid emission pollution and waste of water resources. It can respond to the national call for energy conservation and emission reduction.
  • it can also use the steam pneumatic membrane regulating valve and condensate trap to repair and repair. The pipe continues to feed water, does not delay the operation of the equipment, and has high work efficiency.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Cleaning By Liquid Or Steam (AREA)

Abstract

一种自动化冲洗酒瓶回收装置，其蒸汽加热器（1）的下端通过出水管（23）与调配罐（3）的上端连通，在柠檬酸槽（2）的上端设置有进液管（26），调配罐（3）的下端通过出液管（45）与清洗液储罐（4）的上端连通，清洗液储罐（4）的下端通过出液管（58）与清洗主机（5）的一侧连通，清洗主机（5）的下端通过出液管（62）与混合柠檬酸回收暂存罐（6）的上端连通，混合柠檬酸回收暂存罐（6）的下端通过出液管（66）与粗滤器（7）连通，粗滤器（7）通过出液管（67）与精密过滤器（8）连通，精密过滤器（8）通过出液管（73）与中间储罐（9）的上端连通。该装置自动化程度高，清洗效果好，排污少。

Description

自动化冲洗酒瓶回收装置 技术领域
本发明涉及一种酒瓶清洗设备，尤其涉及一种自动化冲洗酒瓶回收装置。
背景技术
随着饮用酒行业技术标准的逐步提升，饮用酒的质量属于国家强制性的标准，在保证饮用酒内在质量和外观质量不断提高的基础上，同时考虑到生产成本，现在的饮用酒厂大量循环使用回收的酒瓶。而回收酒瓶的利用，必须经过仔细而严谨的清洗过程。在清洗回收酒瓶之前需要先进行清洗液的制备，清洗液一般通过水和酸在一定的温度下调配而成，目前都是通过人工往桶体内按一定比例加水加酸，再对桶体内的水酸混合液加热后形成清洗液，劳动强度大，调配时间长，自动化程度低，温度控制不精确，调配出来的清洗液很难达标，清洗效果差，同时清洗液对酒瓶进行清洗后就直接被排放出去，容易造成酸排放污染和水资源浪费，不能响应国家节能减排的号召。
发明内容
本发明所要解决的技术问题是：提供一种自动化程度高的自动化冲洗酒瓶回收装置。
为了解决上述技术问题，本发明采用的技术方案是：自动化冲洗酒瓶回收装置，包括：蒸汽加热器、柠檬酸槽、调配罐、清洗液储罐、清洗主机、混合 柠檬酸回水暂存罐、粗滤器、精密过滤器和中间储罐，在所述蒸汽加热器内设置有蒸汽加热管，在所述蒸汽加热器的一侧上端设置有与蒸汽加热管相互连通的蒸汽进气主管，在所述蒸汽进气主管上设置有蒸汽气动薄膜调节阀，在所述蒸汽气动薄膜调节阀两侧的蒸汽进气主管上分别设置有第一蒸汽主截止阀和第二蒸汽截止阀，在所述第一蒸汽截止阀和蒸汽气动薄膜调节阀之间的蒸汽进气主管上设置有蒸汽过滤器，在所述蒸汽加热器的一侧下端设置有与蒸汽加热管相互连通的冷凝水出水主管，在所述冷凝水出水主管上设置有冷凝水疏水阀，在所述冷凝水疏水阀两侧的冷凝水出水主管上分别设置有第一冷凝水截止阀和第二冷凝水截止阀，在所述第一冷凝水截止阀和冷凝水疏水阀之间的冷凝水出水主管上设置有冷凝水过滤器，在所述蒸汽加热器的上端设置有与其相互连通的进水管，在所述进水管上设置有进水电磁阀，所述蒸汽加热器的下端通过出水管与调配罐的上端相互连通，在所述进水管和出水管之间的蒸汽加热器内均匀交错设置有若干上导水板和下导水板，所述上导水板的上端与蒸汽加热器相连接，所述上导水板的下端与蒸汽加热器相分离，所述下导水板的下端与蒸汽加热器相连接，所述下导水板的上端与蒸汽加热器相分离，在所述柠檬酸槽的上端设置有柠檬酸进液管，在所述柠檬酸槽的下端设置有柠檬酸槽排污管，在所述柠檬酸槽排污管上设置有柠檬酸槽排污阀，在所述柠檬酸槽的一侧设置有柠檬酸槽磁翻板液位计上下限报警装置，所述柠檬酸槽的下端通过柠檬酸出液管与调配罐相互连通，在所述柠檬酸出液管上设置有柠檬酸离心泵，在所述 柠檬酸离心泵与柠檬酸槽之间的柠檬酸出液管上设置有柠檬酸槽截止阀和柠檬酸槽过滤器，在所述调配罐的上端设置有搅拌电机，所述搅拌电机的电机轴伸入调配罐内与搅拌轴相连接，在所述搅拌轴上设置有若干搅拌叶片，在所述调配罐的下端设置有调配罐排污管，在所述调配罐排污管上设置有调配罐排污阀，在所述调配罐的一侧设置有调配罐磁翻板液位计上下限报警装置，在所述调配罐的另一侧上端设置有调配罐溢流口，所述调配罐溢流口的位置高于调配罐磁翻板液位计上下限报警装置的上限位，所述调配罐溢流口通过调配罐回流管与进水电磁阀和蒸汽加热器之间的进水管相互连通，在所述调配罐回流管上设置有调配罐回流泵，在所述调配罐的另一侧下端设置有测温装置和电导热仪，所述测温装置通过第一导线与蒸汽气动薄膜调节阀相连接，所述电导热仪通过第二导线与柠檬酸离心泵相连接，所述调配罐的下端通过调配罐出液管与清洗液储罐的上端相互连通，在所述调配罐出液管上设置有调配罐出液泵，在所述调配罐出液泵与调配罐之间的调配罐出液管上设置有调配罐截止阀和调配罐过滤器，在所述调配罐出液泵与清洗液储罐之间的调配罐出液管上设置有调配液电磁阀，所述调配罐出液泵通过第三导线与调配罐磁翻板液位计上下限报警装置相连接，在所述清洗液储罐的下端设置有清洗液储罐排污管，在所述清洗液储罐排污管上设置有清洗液储罐排污阀，在所述清洗液储罐的一侧设置有清洗液储罐磁翻板液位计上下限报警装置，所述清洗液储罐磁翻板液位计上下限报警装置通过第四导线与调配罐出液泵相连接，在所述清洗液储罐的另一侧上端设 置有清洗液储罐溢流口，所述清洗液储罐溢流口的位置高于清洗液储罐磁翻板液位计上下限报警装置的上限位，在所述清洗液储罐的另一侧下端设置有取样管，在所述取样管上设置有取样球阀，所述清洗液储罐的下端通过清洗液储罐出液管与清洗主机的一侧相互连通，在所述清洗液储罐出液管上设置有清洗液储罐出液泵，在所述清洗液储罐出液泵与清洗液储罐之间的清洗液储罐出液管上设置有清洗液储罐截止阀和清洗液储罐过滤器，所述清洗主机的下端通过清洗主机出液管与混合柠檬酸回水暂存罐的上端相互连通，在所述混合柠檬酸回水暂存罐的下端设置有混合柠檬酸回水暂存罐排污管，在所述混合柠檬酸回水暂存罐排污管上设置有混合柠檬酸回水暂存罐排污阀，在所述混合柠檬酸回水暂存罐的一侧上端设置有浮球控制装置，所述混合柠檬酸回水暂存罐的下端通过混合柠檬酸回水暂存罐出液管与粗滤器相互连通，所述粗滤器通过粗滤器出液管与精密过滤器相互连通，在所述粗滤器出液管上设置有粗滤器回液泵，所述粗滤器回液泵通过第五导线与浮球控制装置相连接，在所述粗滤器回液泵与粗滤器之间的粗滤器出液管上设置有粗滤器截止阀和粗滤器过滤器，在所述粗滤器回液泵与精密过滤器之间的粗滤器出液管上设置有第一压力表，所述精密过滤器通过精密过滤器出液管与中间储罐的上端相互连通，在所述精密过滤器出液管靠近精密过滤器的一端上设置有第二压力表，所述清洗液储罐溢流口通过清洗液储罐溢流管与第二压力表和中间储罐之间的精密过滤器出液管相互连通，在所述清洗液储罐溢流管上设置有清洗液储罐溢流泵，在所述中间储罐的 下端设置有中间储罐排污管，在所述中间储罐排污管上设置有中间储罐排污阀，在所述中间储罐的一侧设置有中间储罐磁翻板液位计上下限报警装置，所述中间储罐磁翻板液位计上下限报警装置通过第六导线与粗滤器回液泵相连接，所述中间储罐的下端通过中间储罐出液管与进水电磁阀和蒸汽加热器之间的进水管相互连通，在所述中间储罐出液管上设置有中间储罐回液泵，所述中间储罐回液泵通过第七导线与中间储罐磁翻板液位计上下限报警装置相连接，在所述中间储罐回液泵与进水管之间的中间储罐出液管上设置有第一中间储罐电磁阀，所述中间储罐回液泵和进水管之间的中间储罐出液管通过中间储罐回流管与调配罐出液泵和调配液电磁阀之间的调配罐出液管相互连通，在所述中间储罐回流管上设置有第二中间储罐电磁阀。
为了更好地解决上述技术问题，本发明采用的进一步技术方案是：在所述蒸汽进气主管上并联设置有与其相互连通的蒸汽进气副管，在所述蒸汽进气副管上设置有蒸汽副截止阀，所述蒸汽气动薄膜调节阀、第一蒸汽主截止阀、第二蒸汽截止阀和蒸汽过滤器位于蒸汽进气副管两端之间的蒸汽进气主管上。
为了更好地解决上述技术问题，本发明采用的进一步技术方案是：在所述冷凝水出水主管上并联设置有与其相互连通的冷凝水出水副管，在所述冷凝水出水副管上设置有冷凝水副截止阀，所述冷凝水疏水阀、第一冷凝水截止阀、第二冷凝水截止阀和冷凝水过滤器位于冷凝水出水副管两端之间的冷凝水出水主管上。
本发明的优点是：上述自动化冲洗酒瓶回收装置，能够自动加水加酸，加水过程中实现边加水边加热，通过测温装置随时控制水的温度，通过导热仪随时控制酸的比例，降低了工人的劳动强度，调配时间短、速度快，自动化程度高，温度控制精确，调配出来的清洗液能够始终达到使用标准，清洗效果好，同时清洗液对酒瓶进行清洗后能够进行回收过滤再利用，不会造成酸排放污染和水资源浪费，能够响应国家节能减排的号召，另外在对蒸汽气动薄膜调节阀和冷凝水疏水阀进行检修的同时可以利用副管继续进气出水，不耽误设备运行，工作效率高。
附图说明
图1为本发明自动化冲洗酒瓶回收装置的结构示意图。
图中：1、蒸汽加热器，2、柠檬酸槽，3、调配罐，4、清洗液储罐，5、清洗主机，6、混合柠檬酸回水暂存罐，7、粗滤器，8、精密过滤器，9、中间储罐，10、蒸汽加热管，11、蒸汽进气主管，12、蒸汽气动薄膜调节阀，13、第一蒸汽主截止阀，14、第二蒸汽截止阀，15、蒸汽过滤器，16、冷凝水出水主管，17、冷凝水疏水阀，18、第一冷凝水截止阀，19、第二冷凝水截止阀，20、冷凝水过滤器，21、进水管，22、进水电磁阀，23、出水管，24、上导水板，25、下导水板，26、柠檬酸进液管，27、柠檬酸槽排污管，271、柠檬酸槽排污阀，272、柠檬酸槽磁翻板液位计上下限报警装置，28、柠檬酸出液管，29、柠檬酸离心泵，30、柠檬酸槽截止阀，31、柠檬酸槽过滤器，32、搅拌电机，33、 搅拌轴，34、搅拌叶片，35、调配罐排污管，36、调配罐排污阀，37、调配罐磁翻板液位计上下限报警装置，38、调配罐溢流口，39、调配罐回流管，40、调配罐回流泵，41、测温装置，42、电导热仪，43、第一导线，44、第二导线，45、调配罐出液管，46、调配罐出液泵，47、调配罐截止阀，48、调配罐过滤器，49、调配液电磁阀，50、第三导线，51、清洗液储罐排污管，52、清洗液储罐排污阀，53、清洗液储罐磁翻板液位计上下限报警装置，54、第四导线，55、清洗液储罐溢流口，56、取样管，57、取样球阀，58、清洗液储罐出液管，59、清洗液储罐出液泵，60、清洗液储罐截止阀，61、清洗液储罐过滤器，62、清洗主机出液管，63、混合柠檬酸回水暂存罐排污管，64、混合柠檬酸回水暂存罐排污阀，65、浮球控制装置，66、柠檬酸回水暂存罐出液管，67、粗滤器出液管，68、粗滤器回液泵，69、第五导线，70、粗滤器截止阀，71、粗滤器过滤器，72、第一压力表，73、精密过滤器出液管，74、精密过滤器排污管，75、精密过滤器排污球阀，76、第二压力表，77、清洗液储罐溢流管，78、清洗液储罐溢流泵，79、中间储罐排污管，80、中间储罐排污阀，81、中间储罐磁翻板液位计上下限报警装置，82、第六导线，83、中间储罐出液管，84、中间储罐回液泵，85、第七导线，86、第一中间储罐电磁阀，87、中间储罐回流管，88、第二中间储罐电磁阀，89、蒸汽进气副管，90、蒸汽副截止阀，91、冷凝水出水副管，92、冷凝水副截止阀。
具体实施方式
下面结合附图和具体实施例详细描述一下本发明的具体内容。
如图1所示，自动化冲洗酒瓶回收装置，包括：蒸汽加热器1、柠檬酸槽2、调配罐3、清洗液储罐4、清洗主机5、混合柠檬酸回水暂存罐6、粗滤器7、精密过滤器8和中间储罐9，在所述蒸汽加热器1内设置有蒸汽加热管10，在所述蒸汽加热器1的一侧上端设置有与蒸汽加热管10相互连通的蒸汽进气主管11，在所述蒸汽进气主管11上设置有蒸汽气动薄膜调节阀12，在所述蒸汽气动薄膜调节阀12两侧的蒸汽进气主管11上分别设置有第一蒸汽主截止阀13和第二蒸汽截止阀14，在所述第一蒸汽截止阀13和蒸汽气动薄膜调节阀12之间的蒸汽进气主管11上设置有蒸汽过滤器15，在所述蒸汽加热器1的一侧下端设置有与蒸汽加热管10相互连通的冷凝水出水主管16，在所述冷凝水出水主管16上设置有冷凝水疏水阀17，在所述冷凝水疏水阀17两侧的冷凝水出水主管16上分别设置有第一冷凝水截止阀18和第二冷凝水截止阀19，在所述第一冷凝水截止阀18和冷凝水疏水阀17之间的冷凝水出水主管16上设置有冷凝水过滤器20，在所述蒸汽加热器1的上端设置有与其相互连通的进水管21，在所述进水管21上设置有进水电磁阀22，所述蒸汽加热器1的下端通过出水管23与调配罐3的上端相互连通，在所述进水管21和出水管23之间的蒸汽加热器1内均匀交错设置有若干上导水板24和下导水板25，所述上导水板24的上端与蒸汽加热器1相连接，所述上导水板24的下端与蒸汽加热器1相分离，所述下导水板25的下端与蒸汽加热器1相连接，所述下导水板25的上端与蒸汽加热器1 相分离，在所述柠檬酸槽2的上端设置有柠檬酸进液管26，在所述柠檬酸槽2的下端设置有柠檬酸槽排污管27，在所述柠檬酸槽排污管27上设置有柠檬酸槽排污阀271，在所述柠檬酸槽2的一侧设置有柠檬酸槽磁翻板液位计上下限报警装置272，所述柠檬酸槽2的下端通过柠檬酸出液管28与调配罐3相互连通，在所述柠檬酸出液管28上设置有柠檬酸离心泵29，在所述柠檬酸离心泵29与柠檬酸槽2之间的柠檬酸出液管28上设置有柠檬酸槽截止阀30和柠檬酸槽过滤器31，在所述调配罐3的上端设置有搅拌电机32，所述搅拌电机32的电机轴伸入调配罐3内与搅拌轴33相连接，在所述搅拌轴33上设置有若干搅拌叶片34，在所述调配罐3的下端设置有调配罐排污管35，在所述调配罐排污管35上设置有调配罐排污阀36，在所述调配罐3的一侧设置有调配罐磁翻板液位计上下限报警装置37，在所述调配罐3的另一侧上端设置有调配罐溢流口38，所述调配罐溢流口38的位置高于调配罐磁翻板液位计上下限报警装置37的上限位，所述调配罐溢流口38通过调配罐回流管39与进水电磁阀22和蒸汽加热器1之间的进水管21相互连通，在所述调配罐回流管39上设置有调配罐回流泵40，在所述调配罐3的另一侧下端设置有测温装置41和电导热仪42，所述测温装置41通过第一导线43与蒸汽气动薄膜调节阀12相连接，所述电导热仪42通过第二导线44与柠檬酸离心泵29相连接，所述调配罐3的下端通过调配罐出液管45与清洗液储罐4的上端相互连通，在所述调配罐出液管45上设置有调配罐出液泵46，在所述调配罐出液泵46与调配罐3之间的调配罐出液管45 上设置有调配罐截止阀47和调配罐过滤器48，在所述调配罐出液泵46与清洗液储罐4之间的调配罐出液管45上设置有调配液电磁阀49，所述调配罐出液泵46通过第三导线50与调配罐磁翻板液位计上下限报警装置37相连接，在所述清洗液储罐4的下端设置有清洗液储罐排污管51，在所述清洗液储罐排污管51上设置有清洗液储罐排污阀52，在所述清洗液储罐4的一侧设置有清洗液储罐磁翻板液位计上下限报警装置53，所述清洗液储罐磁翻板液位计上下限报警装置53通过第四导线54与调配罐出液泵46相连接，在所述清洗液储罐4的另一侧上端设置有清洗液储罐溢流口55，所述清洗液储罐溢流口55的位置高于清洗液储罐磁翻板液位计上下限报警装置53的上限位，在所述清洗液储罐4的另一侧下端设置有取样管56，在所述取样管56上设置有取样球阀57，所述清洗液储罐4的下端通过清洗液储罐出液管58与清洗主机5的一侧相互连通，在所述清洗液储罐出液管58上设置有清洗液储罐出液泵59，在所述清洗液储罐出液泵59与清洗液储罐4之间的清洗液储罐出液管58上设置有清洗液储罐截止阀60和清洗液储罐过滤器61，所述清洗主机5的下端通过清洗主机出液管62与混合柠檬酸回水暂存罐6的上端相互连通，在所述混合柠檬酸回水暂存罐6的下端设置有混合柠檬酸回水暂存罐排污管63，在所述混合柠檬酸回水暂存罐排污管63上设置有混合柠檬酸回水暂存罐排污阀64，在所述混合柠檬酸回水暂存罐6的一侧上端设置有浮球控制装置65，所述混合柠檬酸回水暂存罐6的下端通过混合柠檬酸回水暂存罐出液管66与粗滤器7相互连通，所述粗滤器7通过粗滤 器出液管67与精密过滤器8相互连通，在所述粗滤器出液管67上设置有粗滤器回液泵68，所述粗滤器回液泵68通过第五导线69与浮球控制装置65相连接，在所述粗滤器回液泵68与粗滤器7之间的粗滤器出液管67上设置有粗滤器截止阀70和粗滤器过滤器71，在所述粗滤器回液泵68与精密过滤器8之间的粗滤器出液管67上设置有第一压力表72，所述精密过滤器8通过精密过滤器出液管73与中间储罐9的上端相互连通，在所述精密过滤器出液管73靠近精密过滤器8的一端上设置有第二压力表76，所述清洗液储罐溢流口55通过清洗液储罐溢流管77与第二压力表76和中间储罐9之间的精密过滤器出液管73相互连通，在所述清洗液储罐溢流管77上设置有清洗液储罐溢流泵78，在所述中间储罐9的下端设置有中间储罐排污管79，在所述中间储罐排污管79上设置有中间储罐排污阀80，在所述中间储罐9的一侧设置有中间储罐磁翻板液位计上下限报警装置81，所述中间储罐磁翻板液位计上下限报警装置81通过第六导线82与粗滤器回液泵68相连接，所述中间储罐9的下端通过中间储罐出液管83与进水电磁阀22和蒸汽加热器1之间的进水管21相互连通，在所述中间储罐出液管83上设置有中间储罐回液泵84，所述中间储罐回液泵84通过第七导线85与中间储罐磁翻板液位计上下限报警装置81相连接，在所述中间储罐回液泵84与进水管21之间的中间储罐出液管83上设置有第一中间储罐电磁阀86，所述中间储罐回液泵84和进水管21之间的中间储罐出液管83通过中间储罐回流管87与调配罐出液泵46和调配液电磁阀49之间的调配罐出液管45相互连通，在 所述中间储罐回流管87上设置有第二中间储罐电磁阀88。
如图1所示，在本实例中，在所述蒸汽进气主管11上并联设置有与其相互连通的蒸汽进气副管89，在所述蒸汽进气副管89上设置有蒸汽副截止阀90，所述蒸汽气动薄膜调节阀12、第一蒸汽主截止阀13、第二蒸汽截止阀14和蒸汽过滤器15位于蒸汽进气副管89两端之间的蒸汽进气主管11上。
如图1所示，在本实例中，在所述冷凝水出水主管16上并联设置有与其相互连通的冷凝水出水副管91，在所述冷凝水出水副管91上设置有冷凝水副截止阀92，所述冷凝水疏水阀17、第一冷凝水截止阀18、第二冷凝水截止阀19和冷凝水过滤器20位于冷凝水出水副管91两端之间的冷凝水出水主管16上。
上述自动化冲洗酒瓶回收装置使用时，同时打开蒸汽进气主管11上的蒸汽气动薄膜调节阀12、第一蒸汽主截止阀13、第二蒸汽主截止阀14和进水管21上的进水电磁阀22，水从进水管21进入到蒸汽加热器1内，蒸汽从蒸汽进气主管11进入到蒸汽加热器1内的蒸汽加热管10内，蒸汽过滤器15可以对蒸汽进行过滤，蒸汽将热量通过蒸汽加热管10传递到蒸汽加热器1内对流经的水进行加热，蒸汽加热后产生的冷凝水可通过打开冷凝水疏水阀17、第一冷凝水截止阀18和第二冷凝水截止阀19经冷凝水出水主管16排出，冷凝水过滤器20可以对冷凝水进行过滤，经过蒸汽加热器1内被加热后的水通过出水管23进入到调配罐3内，打开柠檬酸离心泵29和柠檬酸槽截止阀30，柠檬酸槽2内的柠檬酸通过柠檬酸出液管28和柠檬酸离心泵29进入到调配罐3内，测温装置41随 时检测调配罐3内水酸混合液的温度，当温度低于60℃时，测温装置41将温度信号传递给控制装置，控制装置通过第一导线43控制蒸汽气动薄膜调节阀12提供更大流量的蒸汽，从而使经过蒸汽加热器1内的水被升温，当温度高于60℃时，测温装置41将温度信号传递给控制装置，控制装置通过第一导线43控制蒸汽气动薄膜调节阀12提供更小流量的蒸汽，从而使经过蒸汽加热器1内的水被降温；电导热仪42随时检测调配罐3内水酸混合液的酸度，当酸度过低时，电导热仪42将信号传递给控制装置，控制装置将信号通过第二导线44控制柠檬酸离心泵29打开，柠檬酸继续进入调配罐3内，当酸度过高时，电导热仪42将信号传递给控制装置，控制装置将信号通过第二导线44控制柠檬酸离心泵29关闭，柠檬酸停止进入调配罐3内；启动搅拌电机32，搅拌电机32的电机轴带动搅拌轴33转动，搅拌轴33带动搅拌叶片34转动对调配罐3内的混合液进行搅拌调配，当调配罐3内的液位达到调配罐磁翻板液位计上下限报警装置37的下限位时，调配罐磁翻板液位计上下限报警装置37报警并将信号传递给控制装置，控制装置通过第三导线50控制调配罐出液泵46关闭，调配罐3内的清洗液停止进入清洗液储罐4内，当调配罐3内的液位达到调配罐磁翻板液位计上下限报警装置37的上限位时，调配罐磁翻板液位计上下限报警装置37报警并将信号传递给控制装置，控制装置通过第三导线50控制调配罐出液泵46打开，调配罐3内的清洗液继续进入清洗液储罐4内，当调配罐3内的混合液超过调配罐磁翻板液位计上下限报警装置37的上限位并从调配罐溢流口38处溢出时， 启动调配罐回流泵40将调配罐溢流口38处溢流出来的混合液重新送入到进水管21处进行回流，溢流的混合液可以重新和水一起进入调配罐3内，当调配罐出液泵46被打开时，同时打开调配罐截止阀47和调配液电磁阀49，调配罐3内调配好的清洗液通过调配罐出液管45进入到清洗液储罐4内，调配罐过滤器48可以对经过调配罐出液管45内的清洗液进行过滤；打开取样球阀57，可以通过取样管56将清洗液储罐4内的清洗液取出进行检测，当清洗液储罐4内的清洗液达到清洗液储罐磁翻板液位计上下限报警装置53的下限位时，清洗液储罐磁翻板液位计上下限报警装置53报警并将信号传递给控制装置，控制装置可以通过第四导线54控制调配罐出液泵46打开，调配罐3内的清洗液继续进入清洗液储罐4内，当清洗液储罐4内的清洗液达到清洗液储罐磁翻板液位计上下限报警装置53的上限位时，清洗液储罐磁翻板液位计上下限报警装置53报警并将信号传递给控制装置，控制装置可以通过第四导线54控制调配罐出液泵46关闭，调配罐3内的清洗液停止进入清洗液储罐4内，当清洗液储罐4内的清洗液超过清洗液达到清洗液储罐磁翻板液位计上下限报警装置53的上限位并从清洗液储罐溢流口55溢出时，启动清洗液储罐溢流泵78将从清洗液储罐溢流口55溢出的清洗液通过清洗液储罐溢流管77和精密过滤器出液管73送入到中间储罐9内，当清洗液储罐出液泵59打开时，同时打开清洗液储罐截止阀60，清洗液储罐4内的清洗液被送入到清洗主机5内对酒瓶进行清洗，清洗后的混合柠檬酸水通过清洗主机出液管62进入到混合柠檬酸回水暂存罐6内，当混合 柠檬酸回水暂存罐6内混合柠檬酸水的液位达到一定高度时，通过浮球控制装置65将信号传递给控制装置，控制装置通过第五导线69控制粗滤器回液泵68打开，同时打开粗过滤器截止阀70，混合柠檬酸回水暂存罐6内混合柠檬酸水依次经过柠檬酸回水暂存罐出液管66、粗滤器7、粗滤器出液管67、精密过滤器8和精密过滤器出液管73到达中间储罐9内，粗滤器7对混合柠檬酸水进行大颗粒过滤，粗滤器过滤器71可以对经过粗滤器出液管67的混合液进行再次过滤，精密过滤器8可以对经过两次过滤后的混合液进行精密过滤，经过三次过滤后的清洗液进入中间储罐9内；当中间储罐9内的清洗液达到中间储罐磁翻板液位计上下限报警装置81的下限位时，中间储罐磁翻板液位计上下限报警装置81将信号传递给控制装置，控制装置通过第六导线82控制粗滤器回液泵68打开，当中间储罐9内的清洗液达到中间储罐磁翻板液位计上下限报警装置81的上限位时，中间储罐磁翻板液位计上下限报警装置81将信号传递给控制装置，控制装置通过第七导线85控制中间储罐回液泵84打开，当第一中间储罐电磁阀86打开、第二中间储罐电磁阀88关闭时，中间储罐9内的清洗液直接通过中间储罐出液管83重新送入到进水管21处进行回流可以重新和水一起进入调配罐3内，当第一中间储罐电磁阀86和第二中间储罐电磁阀88同时打开时，由于进水管21的位置远远高于中间储罐回流管87，中间储罐9内的清洗液通过中间储罐出液管83和中间储罐回流管87回流到调配罐出液管45处跟随调配罐3内的清洗液一起进入到清洗液储罐4内；打开柠檬酸槽排污阀271可以 将柠檬酸槽2内沉淀的杂质通过柠檬酸槽排污管27排出，打开调配罐排污阀36可以将调配罐3内沉定的杂质通过调配罐排污管35排出，打开清洗液储罐排污阀52可以将清洗液储罐4内沉淀的杂质通过清洗液储罐排污管51排出，打开混合柠檬酸回水暂存罐排污阀64将混合柠檬酸回水暂存罐6内沉淀的杂质通过混合柠檬酸回水暂存罐排污管63排出，打开中间储罐排污阀80可以将中间储罐9内沉淀的杂质通过中间储罐排污管79排出。
上述自动化冲洗酒瓶回收装置对蒸汽气动薄膜调节阀12进行检修时，同时关闭蒸汽进气主管11上的第一蒸汽主截止阀13和第二蒸汽主截止阀14，打开蒸汽进气副管89上的蒸汽副截止阀90，蒸汽可以继续从蒸汽进气副管89进入到蒸汽加热器1内的蒸汽加热管10，在维修更换蒸汽气动薄膜调节阀12的同时可以保证设备的正常运行。
上述自动化冲洗酒瓶回收装置对冷凝水疏水阀17进行检修时，同时关闭第一冷凝水截止阀18和第二冷凝水截止阀19，打开冷凝水出水副管91上的冷凝水副截止阀92,，冷凝水可以从冷凝水出水副管91排出，在维修更换冷凝水疏水阀17的同时可以保证设备的正常运行。
上述自动化冲洗酒瓶回收装置，能够自动加水加酸，加水过程中实现边加水边加热，通过测温装置随时控制水的温度，通过导热仪随时控制酸的比例，降低了工人的劳动强度，调配时间短、速度快，自动化程度高，温度控制精确，调配出来的清洗液能够始终达到使用标准，清洗效果好，同时清洗液对酒瓶进 行清洗后能够进行回收过滤再利用，不会造成酸排放污染和水资源浪费，能够响应国家节能减排的号召，另外在对蒸汽气动薄膜调节阀和冷凝水疏水阀进行检修的同时可以利用副管继续进气出水，不耽误设备运行，工作效率高。

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  1. 自动化冲洗酒瓶回收装置，其特征在于：包括：蒸汽加热器(1)、柠檬酸槽(2)、调配罐(3)、清洗液储罐(4)、清洗主机(5)、混合柠檬酸回水暂存罐(6)、粗滤器(7)、精密过滤器(8)和中间储罐(9)，在所述蒸汽加热器(1)内设置有蒸汽加热管(10)，在所述蒸汽加热器(1)的一侧上端设置有与蒸汽加热管(10)相互连通的蒸汽进气主管(11)，在所述蒸汽进气主管(11)上设置有蒸汽气动薄膜调节阀(12)，在所述蒸汽气动薄膜调节阀(12)两侧的蒸汽进气主管(11)上分别设置有第一蒸汽主截止阀(13)和第二蒸汽截止阀(14)，在所述第一蒸汽截止阀(13)和蒸汽气动薄膜调节阀(12)之间的蒸汽进气主管(11)上设置有蒸汽过滤器(15)，在所述蒸汽加热器(1)的一侧下端设置有与蒸汽加热管(10)相互连通的冷凝水出水主管(16)，在所述冷凝水出水主管(16)上设置有冷凝水疏水阀(17)，在所述冷凝水疏水阀(17)两侧的冷凝水出水主管(16)上分别设置有第一冷凝水截止阀(18)和第二冷凝水截止阀(19)，在所述第一冷凝水截止阀(18)和冷凝水疏水阀(17)之间的冷凝水出水主管(16)上设置有冷凝水过滤器(20)，在所述蒸汽加热器(1)的上端设置有与其相互连通的进水管(21)，在所述进水管(21)上设置有进水电磁阀(22)，所述蒸汽加热器(1)的下端通过出水管(23)与调配罐(3)的上端相互连通，在所述进水管(21)和出水管(23)之间的蒸汽加热器(1)内均匀交错设置有若干上导水板(24)和下导水板(25)，所述上导水板(24)的上 端与蒸汽加热器(1)相连接，所述上导水板(24)的下端与蒸汽加热器(1)相分离，所述下导水板(25)的下端与蒸汽加热器(1)相连接，所述下导水板(25)的上端与蒸汽加热器(1)相分离，在所述柠檬酸槽(2)的上端设置有柠檬酸进液管(26)，在所述柠檬酸槽(2)的下端设置有柠檬酸槽排污管(27)，在所述柠檬酸槽排污管(27)上设置有柠檬酸槽排污阀(271)，在所述柠檬酸槽(2)的一侧设置有柠檬酸槽磁翻板液位计上下限报警装置(272)，所述柠檬酸槽(2)的下端通过柠檬酸出液管(28)与调配罐(3)相互连通，在所述柠檬酸出液管(28)上设置有柠檬酸离心泵(29)，在所述柠檬酸离心泵(29)与柠檬酸槽(2)之间的柠檬酸出液管(28)上设置有柠檬酸槽截止阀(30)和柠檬酸槽过滤器(31)，在所述调配罐(3)的上端设置有搅拌电机(32)，所述搅拌电机(32)的电机轴伸入调配罐(3)内与搅拌轴(33)相连接，在所述搅拌轴(33)上设置有若干搅拌叶片(34)，在所述调配罐(3)的下端设置有调配罐排污管(35)，在所述调配罐排污管(35)上设置有调配罐排污阀(36)，在所述调配罐(3)的一侧设置有调配罐磁翻板液位计上下限报警装置(37)，在所述调配罐(3)的另一侧上端设置有调配罐溢流口(38)，所述调配罐溢流口(38)的位置高于调配罐磁翻板液位计上下限报警装置(37)的上限位，所述调配罐溢流口(38)通过调配罐回流管(39)与进水电磁阀(22)和蒸汽加热器(1)之间的进水管(21)相互连通，在所述调配罐回流管(39)上设置有调配罐回流泵(40)，在所述调配罐(3)的另一侧下端设置有测温装置(41)和 电导热仪(42)，所述测温装置(41)通过第一导线(43)与蒸汽气动薄膜调节阀(12)相连接，所述电导热仪(42)通过第二导线(44)与柠檬酸离心泵(29)相连接，所述调配罐(3)的下端通过调配罐出液管(45)与清洗液储罐(4)的上端相互连通，在所述调配罐出液管(45)上设置有调配罐出液泵(46)，在所述调配罐出液泵(46)与调配罐(3)之间的调配罐出液管(45)上设置有调配罐截止阀(47)和调配罐过滤器(48)，在所述调配罐出液泵(46)与清洗液储罐(4)之间的调配罐出液管(45)上设置有调配液电磁阀(49)，所述调配罐出液泵(46)通过第三导线(50)与调配罐磁翻板液位计上下限报警装置(37)相连接，在所述清洗液储罐(4)的下端设置有清洗液储罐排污管(51)，在所述清洗液储罐排污管(51)上设置有清洗液储罐排污阀(52)，在所述清洗液储罐(4)的一侧设置有清洗液储罐磁翻板液位计上下限报警装置(53)，所述清洗液储罐磁翻板液位计上下限报警装置(53)通过第四导线(54)与调配罐出液泵(46)相连接，在所述清洗液储罐(4)的另一侧上端设置有清洗液储罐溢流口(55)，所述清洗液储罐溢流口(55)的位置高于清洗液储罐磁翻板液位计上下限报警装置(53)的上限位，在所述清洗液储罐(4)的另一侧下端设置有取样管(56)，在所述取样管(56)上设置有取样球阀(57)，所述清洗液储罐(4)的下端通过清洗液储罐出液管(58)与清洗主机(5)的一侧相互连通，在所述清洗液储罐出液管(58)上设置有清洗液储罐出液泵(59)，在所述清洗液储罐出液泵(59)与清洗液储罐(4)之间的清洗液储罐出液管(58)上设置 有清洗液储罐截止阀(60)和清洗液储罐过滤器(61)，所述清洗主机(5)的下端通过清洗主机出液管(62)与混合柠檬酸回水暂存罐(6)的上端相互连通，在所述混合柠檬酸回水暂存罐(6)的下端设置有混合柠檬酸回水暂存罐排污管(63)，在所述混合柠檬酸回水暂存罐排污管(63)上设置有混合柠檬酸回水暂存罐排污阀(64)，在所述混合柠檬酸回水暂存罐(6)的一侧上端设置有浮球控制装置(65)，所述混合柠檬酸回水暂存罐(6)的下端通过混合柠檬酸回水暂存罐出液管(66)与粗滤器(7)相互连通，所述粗滤器(7)通过粗滤器出液管(67)与精密过滤器(8)相互连通，在所述粗滤器出液管(67)上设置有粗滤器回液泵(68)，所述粗滤器回液泵(68)通过第五导线(69)与浮球控制装置(65)相连接，在所述粗滤器回液泵(68)与粗滤器(7)之间的粗滤器出液管(67)上设置有粗滤器截止阀(70)和粗滤器过滤器(71)，在所述粗滤器回液泵(68)与精密过滤器(8)之间的粗滤器出液管(67)上设置有第一压力表(72)，所述精密过滤器(8)通过精密过滤器出液管(73)与中间储罐(9)的上端相互连通，在所述精密过滤器出液管(73)靠近精密过滤器(8)的一端上设置有第二压力表(76)，所述清洗液储罐溢流口(55)通过清洗液储罐溢流管(77)与第二压力表(76)和中间储罐(9)之间的精密过滤器出液管(73)相互连通，在所述清洗液储罐溢流管(77)上设置有清洗液储罐溢流泵(78)，在所述中间储罐(9)的下端设置有中间储罐排污管(79)，在所述中间储罐排污管(79)上设置有中间储罐排污阀(80)，在所述中间储罐(9)的一侧设置 有中间储罐磁翻板液位计上下限报警装置(81)，所述中间储罐磁翻板液位计上下限报警装置(81)通过第六导线(82)与粗滤器回液泵(68)相连接，所述中间储罐(9)的下端通过中间储罐出液管(83)与进水电磁阀(22)和蒸汽加热器(1)之间的进水管(21)相互连通，在所述中间储罐出液管(83)上设置有中间储罐回液泵(84)，所述中间储罐回液泵(84)通过第七导线(85)与中间储罐磁翻板液位计上下限报警装置(81)相连接，在所述中间储罐回液泵(84)与进水管(21)之间的中间储罐出液管(83)上设置有第一中间储罐电磁阀(86)，所述中间储罐回液泵(84)和进水管(21)之间的中间储罐出液管(83)通过中间储罐回流管(87)与调配罐出液泵(46)和调配液电磁阀(49)之间的调配罐出液管(45)相互连通，在所述中间储罐回流管(87)上设置有第二中间储罐电磁阀(88)。
  2. 按照权利要求1所述的自动化冲洗酒瓶回收装置，其特征在于：在所述蒸汽进气主管(11)上并联设置有与其相互连通的蒸汽进气副管(89)，在所述蒸汽进气副管(89)上设置有蒸汽副截止阀(90)，所述蒸汽气动薄膜调节阀(12)、第一蒸汽主截止阀(13)、第二蒸汽截止阀(14)和蒸汽过滤器(15)位于蒸汽进气副管(89)两端之间的蒸汽进气主管(11)上。
  3. 按照权利要求1或2所述的冲洗酒瓶回收装置，其特征在于：在所述冷凝水出水主管(6)上并联设置有与其相互连通的冷凝水出水副管(91)，在所述冷凝水出水副管(91)上设置有冷凝水副截止阀(92)，所述冷凝水疏水阀(17)、 第一冷凝水截止阀(18)、第二冷凝水截止阀(19)和冷凝水过滤器(20)位于冷凝水出水副管(91)两端之间的冷凝水出水主管(16)上。
PCT/CN2017/094381 2017-06-19 2017-07-25 自动化冲洗酒瓶回收装置 WO2018232825A1 (zh)

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