Quick-dissolving sugar honey diluting device

Abstract

The utility model discloses a quick-dissolving sugar honey diluting device. The quick-dissolving sugar honey diluting device comprises an interception box, a diluting box, a heat exchange coil, a sugar liquid conveying pipe and a diluting water conveying pipe, the interception box is accommodated in the dilution box; multiple filter holes are formed in the bottom of the interception box; the heat exchange coil pipe is accommodated at the bottom of the dilution tank; the first end of the sugar liquid conveying pipe is communicated with a sugar liquid storage tank pipeline, and the second end extends into the interception box; the first end of the dilution water conveying pipe is communicated with the hot water storage tank through a pipeline, and the second end extends into the sugar liquid conveying pipe; a plurality of mixed punching holes are formed in the side wall of the second end of the dilution water conveying pipe; a sealing bottom is arranged at the second end of the dilution water conveying pipe. The device solves the problem that the sugar blocks are difficult to be independently dissolved in the syrup with the brix of 70-80 BX, prevents the syrup containing sugar blocks from entering the next process, and improves the dissolving effect of the sugar blocks in the syrup.

Description

TECHNICAL FIELD

[0001] The application relates to the technical field, in particular to a quick molasses dilution device. BACKGROUND

[0002] In the existing sugar production process, sugar liquid adheres to the inner wall of the pipeline for conveying the sugar liquid, and the adhered sugar liquid dries to form small sugar blocks. When the pipeline is used to convey sugar liquid again, part of the sugar blocks adhering to the inner wall of the pipeline will flow out with the sugar liquid and mix into the sugar liquid. Since the sugar liquid has a high hammer degree, and the size of the sugar blocks can reach 1-2 cm, the sugar blocks contained in the sugar liquid need to be completely dissolved before the sugar liquid enters a sugar boiling tank, so as to ensure that the sugar boiling product meets the requirements. However, in the existing process, the sugar liquid is mainly subjected to dilution operation to dissolve the contained sugar blocks before entering the sugar tank. However, the dissolving speed of the sugar blocks in the dilution process is slow, which affects the normal dilution operation of the sugar liquid. When part of the sugar blocks is subjected to dilution only once, it is difficult to completely dissolve the sugar blocks, and the sugar blocks still need to be subjected to secondary dissolving treatment, which increases the production cost, wastes materials and increases the labor intensity.

[0003] The information disclosed in the background section is only intended to increase the understanding of the general background of the application and should not be considered as admitting or implying that the information constitutes prior art in any form. SUMMARY

[0004] The application provides a quick molasses dilution device, which solves the problem that sugar blocks are difficult to be dissolved in sugar syrup with a hammer degree of 70-80BX alone, avoids the sugar syrup containing sugar blocks from entering the next process and improves the dissolving effect of the sugar blocks in the sugar syrup.

[0005] The application provides a quick molasses dilution device, which includes a trapping box, a dilution box, a heat exchange coil, a sugar liquid conveying pipe and a dilution water conveying pipe.

[0006] The trapping box is accommodated in the dilution box, and the bottom of the trapping box is provided with a plurality of filter holes.

[0007] The heat exchange coil is accommodated at the bottom of the dilution box.

[0008] The first end of the sugar liquid conveying pipe is in communication with a pipeline of a sugar liquid storage tank, and the second end extends into the trapping box. The first end of the dilution water conveying pipe is in communication with a pipeline of a hot water storage tank, and the second end extends into the sugar liquid conveying pipe. A plurality of mixing holes are formed in the sidewall of the second end of the dilution water conveying pipe. The second end of the dilution water conveying pipe is provided with a bottom cover.

[0009] Preferably, the device further includes a hammer degree detector, a temperature sensor, a liquid level meter and a display. The hammer degree detector, the temperature sensor and the liquid level meter are electrically connected to the display. The display is arranged outside the dilution box.

[0010] The hammer degree detector is arranged on the inner side wall of the intercepting box.

[0011] The temperature sensor and the liquid level meter are arranged on the inner side wall of the dilution box.

[0012] Preferably, the device comprises: a material flow sensor and a material valve; the material flow sensor and the material valve are arranged on the sugar liquid conveying pipe; and the material flow sensor is electrically connected to the display.

[0013] Preferably, the device comprises: a water valve and a flow sensor; the water valve and the flow sensor are arranged on the dilution water conveying pipe; and the flow sensor is electrically connected to the display.

[0014] Preferably, the device comprises: a heating steam valve and an air inlet pipe; one end of the air inlet pipe is connected to the air inlet end of the heat exchange coil, and the other end is connected to the air outlet of the steam generating device; and the heating steam valve is arranged on the air inlet pipe.

[0015] Preferably, the device comprises: a discharge valve and a discharge pipe; one end of the discharge pipe is connected to the dilution box, and the other end is connected to the sugar boiling tank; and the discharge valve is arranged on the discharge pipe.

[0016] Preferably, the diameter of the mixing and punching hole and the filter hole is less than or equal to 10 mm.

[0017] Preferably, the diameter of the sugar liquid conveying pipe is greater than the diameter of the dilution water conveying pipe.

[0018] Preferably, the diameter of the sugar liquid conveying pipe is 89 mm, and the diameter of the dilution water conveying pipe is 37 mm.

[0019] Preferably, the liquid level meter is arranged at the highest liquid level of the dilution box; and the highest liquid level of the dilution box is lower than the top of the intercepting box.

[0020] The beneficial effects that can be produced by the application include:

[0021] 1) The rapid dissolved sand sugar molasses dilution device provided by the application can ensure the material flow entering the sugar boiling tank in a continuous production process, while avoiding small sugar blocks from entering the sugar boiling tank, which is conducive to improving the quality of the sugar syrup after boiling.

[0022] 2) The rapid dissolved sand sugar molasses dilution device provided by the application can ensure the normal sugar liquid flow entering the sugar boiling tank without multiple dissolving of sugar blocks, which is conducive to reducing the processing procedure, improving the processing effect, and reducing the labor intensity. BRIEF DESCRIPTION OF DRAWINGS

[0023] Fig. 1 The main structure of the rapid dissolved sand sugar molasses dilution device in at least one embodiment provided by the application is shown in the figure;

[0024] Fig. 2The quick molasses dilution device in at least one embodiment provided in the application is shown in a perspective view;

[0025] Fig. 3 The module connection diagram in at least one embodiment provided in the application is shown in a perspective view;

[0026] Legend:

[0027] Material flow sensor 1, material valve 2, water valve 4, flow sensor 3, liquid level meter 5, hammer detector 6, temperature sensor 7, heating steam valve 9, discharge valve 10, sugar solution conveying pipe 11, dilution water conveying pipe 12, interception box 13, dilution box 14, heat exchange coil 91, air inlet pipe 92, display 21, filter hole 131, mixing hole 121, bottom sealing 122. DETAILED DESCRIPTION

[0028] In order to make the purpose, technical scheme and advantages of the embodiments of the present application clearer, the technical scheme in the embodiments of the present application will be described clearly and completely below in combination with the drawings in the embodiments of the present application. Obviously, the described embodiments are part of the embodiments of the present application, rather than all the embodiments of the present application. The components of the embodiments of the present application described and shown in the drawings herein can be arranged and designed in various different configurations.

[0029] Therefore, the following detailed description of the embodiments of the present application provided in the drawings is not intended to limit the scope of the claimed present application, but only represents selected embodiments of the present application. Based on the embodiments in the present application, all other embodiments obtained by those of ordinary skill in the art without making creative efforts fall within the scope of the present application.

[0030] The controller used in the present embodiment is a prior structure, and the control circuit can be realized by simple programming of those skilled in the art, which belongs to the common knowledge in the art. Only the use is described, and the control mode and circuit connection are not described in detail.

[0031] The technical means not described in detail in the present application and not used to solve the technical problems of the present application are set according to the common knowledge in the art, and various common knowledge setting modes can be realized.

[0032] Reference Figs. 1-3 The quick molasses dilution device provided in the present application comprises an interception box 13, a dilution box 14, an air inlet pipe 92 and a heat exchange coil 91.

[0033] The intercepting box 13 is arranged on one side of the dilution box 14, and a plurality of filter holes 131 are arranged on the bottom surface of the intercepting box 13; the air inlet pipe 92 and the air outlet end of the heat exchange coil 91 are connected in a pipeline manner, and the air outlet end of the heat exchange coil 91 is connected with the pipeline of the steam recovery tank;

[0034] The heat exchange coil 91 is arranged on the bottom surface of the dilution box 14;

[0035] One end of the sugar liquid conveying pipe 11 is connected with the syrup storage tank, and the other end is arranged in the intercepting box 13; one end of the dilution water conveying pipe 12 is connected with the hot water storage tank, and the other end is arranged in the second end of the sugar liquid conveying pipe 11, and a sealing bottom 122 is arranged on the end surface; a plurality of mixing holes 121 are arranged on the end of the dilution water conveying pipe 12.

[0036] According to the arrangement, the syrup containing sugar blocks can be fully mixed and contacted with the hot water output by the dilution water conveying pipe 12 in the sugar liquid conveying pipe 11, and at the same time, the sugar blocks in the syrup are intercepted by the intercepting box 13 and cannot enter the dilution box 14 before being completely dissolved, thereby avoiding the sugar blocks from entering the next process. It is beneficial to improve the quality of the produced syrup. The heat exchange coil 91 can heat the sugar liquid to prevent caking. The device can be used to process incoming materials with a hammer degree of 70-80BX. A small amount of sugar blocks in such incoming materials are difficult to separate and dissolve separately. The device can prevent the sugar blocks in the syrup from entering the next process, and after dilution in the dilution box 14, the hammer degree of the sugar liquid discharged from the dilution box 14 is 60-65BX, which meets the requirements of the material entering the sugar boiling tank.

[0037] In a specific embodiment, the aperture of the filter holes 131 on the bottom surface of the intercepting box 13 is less than or equal to 10mm, which can filter most of the sugar blocks, and is beneficial to improve the sugar block dissolution efficiency.

[0038] In a specific embodiment, the top of the intercepting box 13 is open. When there are many sugar blocks and the filter holes 131 are blocked, the sugar block solution can be discharged from the top to the dilution box 14, ensuring normal material flow.

[0039] In a specific embodiment, it comprises a liquid level meter 5 and a display 21; the liquid level meter 5 is arranged on the dilution box 14 and is used to detect the liquid level in the dilution box 14. When the liquid level is too high, it indicates that the intercepting box 13 is blocked. At this time, stop adding water, discharge the material in the dilution box 14 to cover the bottom of the intercepting box 13, and then heat the dilution liquid to promote the dissolution of the sugar blocks submerged in the liquid in the dilution box, and then normally feed. The liquid level meter 5 is electrically connected with the display 21 arranged outside the dilution box 14. It is convenient for the operator to observe the change of the liquid level.

[0040] In a specific embodiment, it comprises an air inlet pipe 92 and a heating steam valve 9; one end of the air inlet pipe 92 is connected with the air inlet end of the heat exchange coil 91; and the heating steam valve 9 is arranged on the air inlet pipe 92. The heating steam valve 9 is convenient for controlling the entry of heating steam.

[0041] In a specific embodiment, it comprises a hammer degree detector 6 and a display 21; the hammer degree detector 6 is arranged on the inner wall of the interception tank 13 and is electrically connected with the display 21 arranged outside the dilution tank 14. The operator can monitor the hammer degree of the material in the interception tank 13 in real time and control the opening and closing of each pipeline according to the needs.

[0042] In a specific embodiment, it comprises a flow sensor 3 and a water valve 4; the water valve 4 and the flow sensor 3 are arranged on the dilution water conveying pipe 12 at intervals and are electrically connected with the display 21 arranged outside the dilution tank 14. The operator can monitor the water inflow in real time and control the opening and closing of each pipeline according to the needs.

[0043] In a specific embodiment, it comprises a temperature sensor 7; the temperature sensor 7 is arranged on the inner wall of the dilution tank 14 and is electrically connected with the display 21 arranged outside the dilution tank 14. The operator can monitor the temperature of the material in the dilution tank 14 in real time and control the opening degree of the heating steam valve 9 according to the needs.

[0044] In a specific embodiment, it comprises a discharge pipe and a discharge valve 10; the discharge pipe is arranged on one side of the dilution tank 14; the discharge valve 10 is arranged on the discharge pipe. The extended end of the discharge pipe is connected with the sugar boiling tank for conveying the material to the sugar boiling tank. The discharge valve 10 is a pneumatic half-ball valve.

[0045] In a specific embodiment, it comprises a material flow sensor 1 and a material valve 2; the material flow sensor 1 and the material valve 2 are arranged on the sugar liquid conveying pipe 11 at intervals; the material flow sensor 1 is electrically connected with the display 21 arranged outside the dilution tank 14. The operator can timely adjust and control the material valve 2 according to the feedback result of the material flow sensor 1 to meet the production needs.

[0046] In a specific embodiment, the aperture of the mixing and punching hole 121 is less than or equal to 10 mm.

[0047] In a specific embodiment, the pipe diameter of the sugar liquid conveying pipe 11 is greater than the pipe diameter of the dilution water conveying pipe 12. Specifically, the pipe diameter of the sugar liquid conveying pipe 11 is 89 mm; the pipe diameter of the dilution water conveying pipe 12 is 37 mm.

[0048] In a specific embodiment, the liquid level meter 5 is arranged at the highest liquid level of the dilution tank 14, which is 150 mm lower than the top of the interception tank 13, so as to avoid the dilution tank 14 from pouring water into the interception tank 13.

[0049] In a specific embodiment, the pipe diameter of the heat exchange coil 91 and the air inlet pipe 92 is 45 mm.

[0050] Although the utility model has been explained in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions recorded in the foregoing embodiments or make equivalent replacement to part of the technical features, and any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the utility model shall be included in the protection scope of the utility model.

Claims

1. A rapid molasses dissolving sugar cane juice diluting device characterized by, The device comprises: a trapping tank (13), a dilution tank (14), a heat exchange coil (91), a sugar solution conveying pipe (11), and a dilution water conveying pipe (12); the trapping tank (13) is arranged in the dilution tank (14); and a plurality of filter holes (131) are arranged on the bottom of the trapping tank (13); the heat exchange coil (91) is arranged at the bottom of the dilution tank (14); the first end of the sugar solution conveying pipe (11) is connected with a sugar solution storage tank pipeline, and the second end of the sugar solution conveying pipe (11) is arranged in the trapping tank (13); the first end of the dilution water conveying pipe (12) is connected with a hot water storage tank pipeline, and the second end of the dilution water conveying pipe (12) is arranged in the sugar solution conveying pipe (11); a plurality of mixing holes (121) are arranged on the sidewall of the second end of the dilution water conveying pipe (12); and a bottom cover (122) is arranged on the second end of the dilution water conveying pipe (12).

2. The rapid dissolving of sugar molasses diluting device as claimed in claim 1 wherein, The device comprises: a brix detector (6), a temperature sensor (7), a liquid level meter (5), and a display (21); the brix detector (6), the temperature sensor (7), and the liquid level meter (5) are electrically connected with the display (21); and the display (21) is arranged outside the dilution tank (14); the brix detector (6) is arranged on the inner sidewall of the trapping tank (13); the temperature sensor (7) and the liquid level meter (5) are arranged on the inner sidewall of the dilution tank (14) at intervals.

3. The rapid dissolving of sugar molasses diluting device as claimed in claim 2 wherein, The device comprises: a material flow sensor (1) and a material valve (2); the material flow sensor (1) and the material valve (2) are arranged on the sugar solution conveying pipe (11) at intervals; and the material flow sensor (1) is electrically connected with the display (21).

4. The rapid dissolving of sugar molasses diluting device as claimed in claim 2 wherein, The device comprises: a water valve (4) and a flow sensor (3); the water valve (4) and the flow sensor (3) are arranged on the dilution water conveying pipe (12) at intervals; and the flow sensor (3) is electrically connected with the display (21).

5. The rapid dissolving of sugar molasses diluting device as claimed in claim 1 wherein, The device comprises: a heating steam valve (9) and an air inlet pipe (92); one end of the air inlet pipe (92) is connected with the air inlet end of the heat exchange coil (91), and the other end of the air inlet pipe (92) is connected with the air outlet of a steam generating device; and the heating steam valve (9) is arranged on the air inlet pipe (92).

6. The rapid dissolving of sugar molasses diluting device as claimed in claim 1 wherein, The device comprises: a discharge valve (10) and a discharge pipe; one end of the discharge pipe is connected with the dilution tank (14), and the other end of the discharge pipe is connected with a sugar boiling tank; and the discharge valve (10) is arranged on the discharge pipe.

7. The rapid dissolving of sugar molasses diluting device as claimed in claim 1 wherein, The diameters of the mixing holes (121) and the filter holes (131) are less than or equal to 10 mm.

8. The rapid dissolving of sugar molasses diluting device as claimed in claim 1 wherein, The diameter of the sugar solution conveying pipe (11) is greater than the diameter of the dilution water conveying pipe (12).

9. The rapid dissolving of sugar molasses diluting device as claimed in claim 1 wherein, The diameter of the sugar solution conveying pipe (11) is 89 mm; and the diameter of the dilution water conveying pipe (12) is 37 mm.

10. The rapid dissolving of sugar molasses diluting device as claimed in claim 1 wherein, The liquid level meter (5) is arranged at the highest liquid level of the dilution tank (14); and the highest liquid level of the dilution tank (14) is lower than the top of the trapping tank (13).

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