Sugarcane juice concentration and sugarcane plant water co-production integrated device

Abstract

The utility model provides an integrated device for concentration of sugarcane juice and co-production of sugarcane plant water, which relates to the technical field of deep processing of sugarcane and comprises a preparation section and a purification section which are sequentially connected, the preparation section consists of a first concentration tank, a second concentration tank, a third concentration tank and a fourth concentration tank which are connected in series through pipelines and liquid pipelines with pumps, the steam pipeline is connected with the steam pipeline, so that the preparation of sugarcane juice and the cyclic utilization of heat energy are realized; the purification section comprises a raw water tank, an activated carbon treatment unit, an RO (Reverse Osmosis) treatment unit, a pure water tank, an ozone tower treatment unit and a high-temperature sterilization treatment unit which are sequentially connected along the material flow direction, so that the deep purification of the sugarcane plant water is realized. Through the reasonable structural design and the innovative technical scheme, efficient preparation and deep purification of the sugarcane plant water are achieved, remarkable technical advantages and market competitiveness are achieved, and reliable technical support is provided for large-scale industrial production of the sugarcane plant water.

Description

TECHNICAL FIELD

[0001] The utility model relates to the technical field of sugarcane deep processing, and specifically relates to a sugarcane juice concentration and sugarcane plant water co-production integrated device. BACKGROUND

[0002] Sugarcane, widely cultivated in tropical and subtropical regions, not only plays an important role in the food industry, but also exhibits diverse applications in energy, medicine, agriculture, and other fields. The improvement of planting techniques and innovation of processing technology continuously expand the utilization value of sugarcane. Traditionally, sugarcane is mainly used for sugar production and fresh food, but with the development of technology, its application in biofuels, environmental materials, and other aspects has gradually attracted attention. For example, sugarcane residue is used to manufacture environmentally friendly particles and cultivate edible fungi, while sugarcane leaves can be used as animal feed or to produce paper and fiberboard. In addition, the medicinal value of sugarcane cannot be ignored, as various amino acids and trace elements in its stem juice have certain tonifying effects. In terms of cultivation, selecting appropriate varieties and scientific management methods are crucial for improving the yield and quality of sugarcane. With the in-depth exploration of sugarcane resources, its potential economic and ecological value will be further released, providing new impetus for sustainable development.

[0003] Sugarcane plant water is an innovative natural drink developed by our company in collaboration with university research teams after years of scientific research. It maximally retains the natural nutritional components and unique flavor of sugarcane. Unlike traditional drinks, it is natural, healthy, fresh, soft, and sweet. Its advent not only fills the gap in the domestic sugarcane plant water beverage market, but also provides consumers with a new choice of healthy drinks, meeting the pursuit of modern people for healthy and natural drinks. As a forward-looking product, the development of sugarcane plant water reflects our company's innovative concept of deep development and comprehensive utilization of sugarcane resources, and demonstrates our determination and strength in promoting the development of the sugarcane industry towards high value and diversification.

[0004] Because sugarcane plant water is a new product of our company, on the one hand, there is a lack of specialized technology and devices in existing technology to realize large-scale preparation of sugarcane plant water. At the same time, traditional concentration devices also have certain deficiencies in heat energy utilization, as steam is often directly discharged after use, leading to waste of heat energy, increasing production cost, and making resource utilization rate low. On the other hand, after extraction and preparation of sugarcane plant water, it cannot be directly filled as a product, but also needs a series of processing technology, and there is a lack of specialized technology and devices in existing technology to realize large-scale purification treatment of sugarcane plant water.

[0005] Therefore, a new production device is needed to solve the problems of preparation and purification of sugarcane plant water, accelerate the industrialization of new products, and at the same time, the device should have energy-saving features and adapt to large production needs. [Utility Model Content]

[0006] The purpose of this invention is to address the problem of large-scale sugarcane plant water preparation and purification devices by providing an integrated device for the co-production of sugarcane juice concentration and sugarcane plant water. This production line aims to achieve efficient preparation and deep purification of sugarcane plant water, improve heat energy utilization, reduce production costs, meet the needs of large-scale production, and accelerate the industrialization process of sugarcane plant water.

[0007] To achieve the above objectives, the technical solution adopted by this utility model is as follows:

[0008] An integrated device for sugarcane juice concentration and sugarcane plant aquaculture includes a preparation section and a purification section connected in sequence.

[0009] The preparation section includes a first concentration tank, a second concentration tank, a third concentration tank, and a fourth concentration tank. The upper part of the first concentration tank is connected to the lower part of the second concentration tank via a first pipe. The upper part of the second concentration tank is connected to the inlet of a first condenser via a second pipe. The gas outlet of the first condenser is connected to the lower part of the third concentration tank via a sixth pipe, and the condensate outlet of the first condenser is connected to a collection tank via a fifth pipe. The upper part of the third concentration tank is connected to the inlet of the second condenser via a third pipe. The gas outlet of the second condenser is connected to the lower part of the fourth concentration tank via an eighth pipe, and the condensate outlet of the second condenser is connected to a collection tank via a seventh pipe. The upper part of the fourth concentration tank is connected to the lower part of the first concentration tank via a fourth pipe. The lower parts of the first, second, third, and fourth concentration tanks are connected in series via liquid pipes with pumps and are all connected to steam pipes.

[0010] The purification section includes a raw water tank, an activated carbon treatment unit, an RO reverse osmosis treatment unit, a pure water tank, an ozone tower treatment unit, and a high-temperature sterilization treatment unit connected sequentially along the material flow direction. The inlet of the raw water tank is connected to a delivery pipe, which is connected to the outlet of the collection tank. The activated carbon treatment unit is connected to the outlet of the raw water tank via a second pumped pipe. The inlet of the RO reverse osmosis treatment unit is connected to the outlet of the activated carbon treatment unit via a third pumped pipe, and its product water outlet is connected to the inlet of the pure water tank via a first connecting pipe. The outlet of the pure water tank is connected to the inlet of the ozone tower treatment unit via a fourth pumped pipe. The outlet of the ozone tower treatment unit is connected to the inlet of the high-temperature sterilization treatment unit via a fifth pumped pipe, and the outlet of the high-temperature sterilization treatment unit is connected to an outlet pipe.

[0011] Further optimized, the first concentration tank is equipped with a feed pipe, and the fourth concentration tank is equipped with a discharge pipe.

[0012] Further optimization, the first pipeline, second pipeline, third pipeline and fourth pipeline are provided with three-way valves.

[0013] Further optimization, the conveying pipe is provided with a pump and a valve.

[0014] Further optimization, the first, second, third and fourth concentration tanks are respectively provided with pumps and valves in the liquid pipes between each adjacent tank.

[0015] Further optimization, the fifth and seventh pipelines are provided with filtering devices before the collection tank, and the outlets of the filtering devices are connected with the inlets of the collection tank.

[0016] Further optimization, the first, second, third and fourth pipelines are provided with pressure regulating valves.

[0017] Further optimization, the water inlet end of the RO reverse osmosis treatment unit is also provided with a concentrated water outlet, and the production line device further comprises a reverse cleaning system, the system comprising a hot water unit, an acid washing unit and an alkali washing unit, the hot water unit being connected with the water outlet of the RO reverse osmosis treatment unit through a hot water pipeline; the acid washing unit being connected with the water outlet of the RO reverse osmosis treatment unit through an acid washing pipeline; the alkali washing unit being connected with the water outlet of the RO reverse osmosis treatment unit through an alkali washing pipeline; and the cleaning water of the reverse cleaning system being discharged through the concentrated water outlet.

[0018] Further optimization, the switching valve group is provided between the water outlet and the first connecting pipe, and is also connected with the hot water pipeline, the acid washing pipeline and the alkali washing pipeline.

[0019] Further optimization, the switching valve group is a five-way valve.

[0020] As described above, by adopting the technical scheme, the present application has the following advantages:

[0021] 1. The four-effect distillation concentration device is designed, which realizes large-scale extraction of sugarcane plant water in industry for the first time, adopts a unique pipeline connection and condensate collection method, continuously prepares high-purity sugarcane plant water in industrial production for the first time, proposes to collect the steam condensate generated by the second and third concentration tanks as sugarcane plant water for the first time, and realizes directional enrichment of volatile components in the sugarcane processing process for the first time.

[0022] When the sugarcane plant water is prepared, the design is made according to the characteristics of the sugarcane water, through the sequentially arranged raw water tank, activated carbon treatment unit, RO reverse osmosis treatment unit, pure water tank, ozone tower treatment unit and high-temperature sterilization treatment unit along the material flow direction, the deep purification of the sugarcane plant water is realized. The activated carbon treatment effectively adsorbs organic matter and peculiar smell, the RO reverse osmosis precisely filters impurities and harmful substances, the ozone tower and high-temperature sterilization treatment ensure complete sterilization, the purity and safety of the sugarcane plant water are ensured, and the market requirement of high-quality drinks is met.

[0023] 2. The steam of the fourth concentration tank enters the first concentration tank for preheating, and almost no hot steam is discharged from the whole device, the closed-loop steam circuit design (the fourth concentration tank→the first concentration tank) based on the four-effect concentration tank makes the low-temperature waste heat participate in material preheating, and fundamentally solves the problem of energy waste caused by direct discharge of the last-effect steam in the traditional evaporation system. Compared with the one-way steam process, the design makes the overall thermal efficiency of the system obtain a breakthrough improvement through heat recycling.

[0024] The devices such as the three-way valve, the pump, the valve and the pressure regulating valve arranged on each pipeline make the whole production process flexible to control, easy to operate and stable to run, accurate parameter control can be carried out according to actual production requirements, and the efficient preparation and stable production of the sugarcane plant water are ensured.

[0025] 3. The innovative reverse cleaning system: the specially designed reverse cleaning system includes a hot water unit, an acid washing unit and an alkali washing unit, cleaning water is discharged through a concentrated water outlet, and the efficient cleaning of the RO reverse osmosis treatment unit is realized. The combination mode of acid washing, alkali washing and hot water flushing can effectively remove the pollutants on the membrane surface, prolong the service life of the membrane, reduce the operation cost of the equipment, and ensure the stability of the product quality. BRIEF DESCRIPTION OF DRAWINGS

[0026] Figure 1 It is a structure schematic view of the sugarcane juice concentration and sugarcane plant water combined production integrated device of the utility model;

[0027] Figure 2 It is a structure schematic view of the preparation section of the utility model;

[0028] Figure 3 It is a structure schematic view of another preferable embodiment device of the collection tank of the preparation section of the utility model;

[0029] Figure 4 It is a structure schematic view of the purification section of the utility model;

[0030] Figure 5 It is a structure schematic view of the switch valve group of the purification section of the utility model;

[0031] In the figure: 1 - first concentration tank; 2 - second concentration tank; 3 - third concentration tank; 4 - fourth concentration tank; 7 - collection tank; 8 - vapor pipeline; 11 - delivery pipe, 12 - raw water tank, 13 - activated carbon treatment unit, 14 - hot water unit, 15 - acid washing unit, 16 - alkali washing unit, 17 - RO reverse osmosis treatment unit, 18 - pure water tank, 19 - ozone tower treatment unit, 20 - high temperature sterilization treatment unit, 21 - switching valve group, 51 - first pipeline; 52 - second pipeline; 53 - third pipeline; 54 - fourth pipeline; 55 - fifth pipeline; 56 - sixth pipeline; 57 - seventh pipeline; 58 - eighth pipeline; 61 - first condenser; 62 - second condenser; 71 - filtering device; 91 - liquid pipeline; 92 - feeding pipe; 93 - discharging pipe, 121 - second belt pump pipeline, 131 - third belt pump pipeline, 141 - hot water pipeline, 151 - acid washing pipeline, 161 - alkali washing pipeline, 171 - first connecting pipe, 181 - fourth belt pump pipeline, 191 - fifth belt pump pipeline, 201 - liquid outlet pipe. DETAILED DESCRIPTION

[0032] The technical solutions in the embodiments of the present application will be clearly and completely described below with reference to the drawings in the embodiments of the present application. Obviously, the described embodiments are only part of the embodiments of the present application, rather than all the embodiments. Based on the embodiments in the present application, all other embodiments obtained by those skilled in the art without creative labor fall within the scope of protection of the present application.

[0033] It should be noted that when a component is referred to as being "fixed" to another component, it can be directly on the other component or there can be intervening components. When a component is referred to as being "connected" to another component, it can be directly connected to the other component or there can be intervening components. When a component is referred to as being "disposed" on another component, it can be directly on the other component or there can be intervening components. The terms "vertical", "horizontal", "left", "right", and similar terms as used herein are for purposes of description only.

[0034] Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs. The terminology used in the description of the application herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the application. As used in this description, the term "and / or" includes any and all combinations of one or more of the associated listed items.

[0035] Example 1

[0036] The application discloses a sugarcane juice concentration and sugarcane plant water integrated device, which comprises a preparation section and a purification section connected in sequence.

[0037] The preparation section comprises:

[0038] The first concentration tank 1 is connected with the lower part of the second concentration tank 2 through the first pipeline 51; the upper part of the second concentration tank 2 is connected with the inlet of the first condenser 61 through the second pipeline 52; the gas outlet of the first condenser 61 is connected with the lower part of the third concentration tank 3 through the sixth pipeline 56; the condensate outlet of the first condenser 61 is connected with the collecting tank 7 through the fifth pipeline 55; the upper part of the third concentration tank 3 is connected with the inlet of the second condenser 62 through the third pipeline 53; the gas outlet of the second condenser 62 is connected with the lower part of the fourth concentration tank 4 through the eighth pipeline 58; the condensate outlet of the second condenser 62 is connected with the collecting tank 7 through the seventh pipeline 57; and the upper part of the fourth concentration tank 4 is connected with the lower part of the first concentration tank 1 through the fourth pipeline 54.

[0039] The purification section comprises, in sequence along the material flow direction:

[0040] The raw water tank 12 is connected with the feed pipeline 11 through the inlet;

[0041] The active carbon treatment unit 13 is connected with the outlet of the raw water tank through the second pipeline 121 with a pump;

[0042] The RO reverse osmosis treatment unit 17 is connected with the outlet of the active carbon treatment unit through the water inlet of the third pipeline 131 with a pump, and is connected with the inlet of the pure water tank 18 through the first connecting pipeline 171;

[0043] The pure water tank 18 is connected with the inlet of the ozone tower treatment unit 19 through the outlet of the fourth pipeline 181 with a pump;

[0044] The ozone tower treatment unit 19 is connected with the inlet of the high-temperature sterilization treatment unit 20 through the outlet of the fifth pipeline 191 with a pump;

[0045] The high-temperature sterilization treatment unit 20 is connected with the outlet pipeline 201.

[0046] Example 2

[0047] On the basis of the further optimization of example 1, each steam pipeline 8 connected with the first concentration tank 1, the second concentration tank 2, the third concentration tank 3 and the fourth concentration tank 4 is provided with a control valve or a valve.

[0048] The first concentration tank 1 is provided with a feed pipe 92, and the fourth concentration tank 4 is provided with a discharge pipe 93. The collection tank 7 is provided with a discharge port connected to the conveying pipe 11.

[0049] The first pipe 51, the second pipe 52, the third pipe 53 and the fourth pipe 54 are provided with three-way valves. The conveying pipe 11 is provided with a pump and a valve.

[0050] The liquid pipes 91 between each adjacent tank of the first concentration tank 1, the second concentration tank 2, the third concentration tank 3 and the fourth concentration tank 4 are respectively provided with a pump and a valve.

[0051] The fifth pipe 55 and the seventh pipe 57 are provided with a filtering device 71 before being connected to the collection tank 7, and the outlet of the filtering device 71 is connected to the inlet of the collection tank 7.

[0052] The first pipe 51, the second pipe 52, the third pipe 53 and the fourth pipe 54 are provided with pressure regulating valves.

[0053] Embodiment 3

[0054] Further optimized on the basis of Embodiment 1 or Embodiment 2, in order to realize efficient cleaning of the RO reverse osmosis treatment unit 17, the device further comprises a reverse cleaning system, the water inlet end of the RO reverse osmosis treatment unit 17 is further provided with a concentrated water outlet, and the device further comprises a reverse cleaning system, which comprises a hot water unit 14, an acid washing unit 15 and an alkali washing unit 16. The hot water unit 14 is connected to the water outlet of the RO reverse osmosis treatment unit 17 through a hot water pipe 141. The acid washing unit 15 is connected to the water outlet of the RO reverse osmosis treatment unit 17 through an acid washing pipe 151. The alkali washing unit 16 is connected to the water outlet of the RO reverse osmosis treatment unit 17 through an alkali washing pipe 161. The cleaning water of the reverse cleaning system is discharged through the concentrated water outlet.

[0055] The reverse cleaning system further comprises a switching valve group 21, which is arranged between the water outlet and a first connecting pipe 171, and is further connected to the hot water pipe 141, the acid washing pipe 151 and the alkali washing pipe 161.

[0056] The switching valve group is a five-way valve.

[0057] In specific implementation, first, the sugarcane juice is input into the first concentration tank 1 through the feed pipe 92 of the first concentration tank 1, then steam is input into each concentration tank through the steam pipe 8, the liquid pipe 91 with a pump can pump the sugarcane juice in the upper-stage concentration tank into the lower-stage concentration tank, and the steam heats and concentrates the sugarcane juice. After the sugarcane juice in the fourth concentration tank 4 is concentrated, it is conveyed to the next process through the discharge pipe 93.

[0058] During the heating process, the steam generated by the first concentration tank 1 enters the second concentration tank 2 through the first pipeline 51 to preheat and concentrate the sugarcane juice in the second concentration tank 2. The steam generated by the second concentration tank 2 enters the first condenser 61 through the second pipeline 52 for condensation. The condensed liquid, i.e., sugarcane plant water, flows into the collection tank 7 through the fifth pipeline 55. The uncondensed gas enters the third concentration tank 3 through the sixth pipeline 56 to preheat and concentrate the sugarcane juice in the third concentration tank 3. The steam generated by the third concentration tank 3 enters the second condenser 62 through the third pipeline 53 for condensation. The condensed liquid, i.e., sugarcane plant water, also flows into the collection tank 7. The uncondensed gas enters the fourth concentration tank 4 through the eighth pipeline 58. The steam generated by the fourth concentration tank 4 returns to the first concentration tank 1 through the fourth pipeline 54 for recycling, achieving efficient utilization of heat energy.

[0059] During the entire process, the three-way valves, pumps, valves, and pressure regulating valves on the pipelines can be adjusted and controlled according to actual production conditions to ensure stable and efficient production. The sugarcane plant water in the collection tank 7 can be transported to the next process through the discharge port and the delivery pipe 11 for further processing or packaging. The filtration device 71 can filter the condensed liquid flowing into the collection tank 7 to ensure the purity of the sugarcane plant water.

[0060] The raw sugarcane plant water enters the raw water tank 12 from the collection tank 7 through the delivery pipe 11, is temporarily stored, and then flows into the activated carbon treatment unit 13 in sequence. The activated carbon's adsorption property is used to remove organic matter and odors. Then, the water enters the RO reverse osmosis treatment unit 17, which retains and removes most of the dissolved salts, small-molecule organic matter, bacteria, viruses, and other impurities in the water, obtaining high-purity sugarcane plant water. The purified water after RO reverse osmosis treatment flows into the purified water tank 18 for temporary storage and is transported to the ozone tower treatment unit 19 through the fourth pump pipeline 181. The strong oxidizing property of ozone is used to kill residual bacteria, viruses, and other microorganisms, decompose organic pollutants, and further improve water quality. The sugarcane plant water after ozone treatment enters the high-temperature sterilization treatment unit 20 for heating and sterilization, completely killing residual microorganisms to ensure that the product meets commercial sterile standards, and then can enter the next process such as the filling process.

[0061] When the RO reverse osmosis treatment unit 17 needs to be cleaned, the switching valve group 21 (five-way valve) is used to switch between different cleaning modes. During normal operation, the water flows through the water outlet and the first connecting pipe 171 into the subsequent treatment unit. When cleaning is needed, the switching valve group connects the water outlet with one of the hot water unit 14, the acid washing unit 15, and the alkali washing unit 16, respectively, so that the cleaning liquid flows into the RO reverse osmosis treatment unit 17 in the reverse direction to complete the acid washing, alkali washing, or hot water flushing operation, removing the pollutants on the membrane surface, and extending the service life of the membrane.

[0062] The above description is directed to the detailed description of the preferred feasible embodiment of the present application, but the embodiment is not used to limit the patent application range of the present application, and any equivalent change or modification change completed under the technical spirit of the present application should belong to the patent range covered by the present application.

Claims

1. A sugarcane juice concentration and sugarcane plant water integrated production device, characterized by, The preparation section and the purification section are connected in sequence, The preparation section comprises: a first concentration tank, a second concentration tank, a third concentration tank and a fourth concentration tank, the upper part of the first concentration tank is connected with the lower part of the second concentration tank through a first pipeline, the upper part of the second concentration tank is connected with the inlet of a first condenser through a second pipeline, the gas outlet of the first condenser is connected with the lower part of the third concentration tank through a sixth pipeline, the condensate outlet of the first condenser is connected with a collection tank through a fifth pipeline, the upper part of the third concentration tank is connected with the inlet of a second condenser through a third pipeline, the gas outlet of the second condenser is connected with the lower part of the fourth concentration tank through an eighth pipeline, the condensate outlet of the second condenser is connected with the collection tank through a seventh pipeline, the upper part of the fourth concentration tank is connected with the lower part of the first concentration tank through a fourth pipeline, the lower parts of the first concentration tank, the second concentration tank, the third concentration tank and the fourth concentration tank are connected in sequence through liquid pipelines with pumps, and are connected with a vapor pipeline; The purification section comprises, in sequence along the material flow direction, a raw water tank, an activated carbon treatment unit, an RO reverse osmosis treatment unit, a pure water tank, an ozone tower treatment unit and a high-temperature sterilization treatment unit, the inlet of the raw water tank is connected with a conveying pipeline which is connected with the outlet of the collection tank, the activated carbon treatment unit is connected with the outlet of the raw water tank through a second pipeline with a pump, the water inlet of the RO reverse osmosis treatment unit is connected with the outlet of the activated carbon treatment unit through a third pipeline with a pump, the water outlet of the RO reverse osmosis treatment unit is connected with the inlet of the pure water tank through a first connecting pipeline, the outlet of the pure water tank is connected with the inlet of the ozone tower treatment unit through a fourth pipeline with a pump, the outlet of the ozone tower treatment unit is connected with the inlet of the high-temperature sterilization treatment unit through a fifth pipeline with a pump, and the outlet of the high-temperature sterilization treatment unit is connected with a liquid outlet pipeline.

2. A device for integrated production of concentrated sugarcane juice and water from sugarcane plants as claimed in claim 1, wherein, The first concentration tank is provided with a feeding pipeline, and the fourth concentration tank is provided with a discharging pipeline.

3. A device for integrated production of concentrated sugarcane juice and water from sugarcane plants as claimed in claim 1, wherein, Three-way valves are arranged on the first pipeline, the second pipeline, the third pipeline and the fourth pipeline.

4. A device for integrated production of concentrated sugarcane juice and water from sugarcane plants as claimed in claim 1, wherein, A pump and a valve are arranged on the conveying pipeline.

5. A device for integrated production of concentrated sugarcane juice and water from sugarcane plants as claimed in claim 1, wherein, A pump and a valve are arranged on the liquid pipeline between each adjacent tank of the first concentration tank, the second concentration tank, the third concentration tank and the fourth concentration tank.

6. A device for integrated production of sugarcane juice concentrate and water from sugarcane plant as claimed in claim 1 wherein, A filtering device is arranged on the fifth pipeline and the seventh pipeline before the filtering device is connected with the inlet of the collection tank.

7. A device for integrated production of sugarcane juice concentrate and water from sugarcane plant as claimed in claim 1 wherein, Pressure regulating valves are arranged on the first pipeline, the second pipeline, the third pipeline and the fourth pipeline.

8. A device for integrated production of sugarcane juice concentrate and water from sugarcane plant as claimed in claim 1 wherein, The water inlet end of the RO reverse osmosis treatment unit is further provided with a concentrated water outlet, and the production line device further comprises a reverse cleaning system, the reverse cleaning system comprises a hot water unit, an acid cleaning unit and an alkali cleaning unit, the hot water unit is connected with the water outlet of the RO reverse osmosis treatment unit through a hot water pipeline, the acid cleaning unit is connected with the water outlet of the RO reverse osmosis treatment unit through an acid cleaning pipeline, the alkali cleaning unit is connected with the water outlet of the RO reverse osmosis treatment unit through an alkali cleaning pipeline, and the cleaning water of the reverse cleaning system is discharged through the concentrated water outlet.

9. A device for integrated production of sugar cane juice concentrate and sugar cane plant water according to claim 8, characterized in that, A switching valve group is further arranged between the water outlet and the first connecting pipeline, and the switching valve group is further connected with the hot water pipeline, the acid cleaning pipeline and the alkali cleaning pipeline.

10. A device for integrated production of sugar cane juice concentrate and sugar cane plant water according to claim 9, characterized in that, The switching valve group is a five-way valve.

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