CN211430970U - Be applied to decoloration hydrolysis equipment of preparation marine alga dietary fiber - Google Patents

Be applied to decoloration hydrolysis equipment of preparation marine alga dietary fiber Download PDF

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Publication number
CN211430970U
CN211430970U CN201921977261.3U CN201921977261U CN211430970U CN 211430970 U CN211430970 U CN 211430970U CN 201921977261 U CN201921977261 U CN 201921977261U CN 211430970 U CN211430970 U CN 211430970U
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pipe
decoloration
hydrolysis
dietary fiber
hydrolysis tank
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CN201921977261.3U
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Chinese (zh)
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于大洋
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Yantai Zhouji Marine Biological Technology Co ltd
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Yantai Zhouji Marine Biological Technology Co ltd
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Abstract

The utility model discloses a be applied to preparation marine alga dietary fiber's decoloration hydrolysis equipment, including decoloration hydrolysis tank, delivery pump, heat transfer mechanism, temperature control mechanism is connected to decoloration hydrolysis tank one side, conveying mechanism is connected to decoloration hydrolysis tank upper end, conveying mechanism one end is provided with detection mechanism, decoloration hydrolysis tank lower extreme connection auxiliary material mechanism. The utility model discloses rational in infrastructure, the device adopts external energy and disk heat pipe to heat and refrigerate, has improved accuse temperature efficiency, utilizes the heat exchanger to carry out rapid cooling to the material simultaneously, improves cooling efficiency, and easy operation utilizes external control ware to connect the electrical apparatus, realizes automated control and processing, has improved accuracy and work efficiency, and the security is high, can real time monitoring reaction state through detection mechanism, guarantees the utilization ratio of inside material and operating personnel's safety.

Description

Be applied to decoloration hydrolysis equipment of preparation marine alga dietary fiber
Technical Field
The utility model relates to a marine alga dietary fiber preparation field especially relates to a be applied to preparation marine alga dietary fiber's decoloration hydrolysis equipment.
Background
Dietary fiber is defined as the sum of edible plant cells, polysaccharides, lignin and related substances, wherever they are not digested and absorbed by endogenous enzymes in the human body. This definition includes a number of components in food products: cellulose, hemicellulose, oligosaccharides, lignin, lipidoids, pectin, modified cellulose, mucilage, and oligosaccharides. Dietary fiber is a heterogeneous group of complex natural macromolecular substances.
In the process of preparing the dietary fiber, the dietary fiber is required to be decolorized and hydrolyzed, common reaction equipment is prepared by utilizing a common reaction tank, the preparation process needs to be observed and controlled in time, the internal temperature needs to be accurately controlled, otherwise, the preparation process is influenced, and the working difficulty of workers is greatly increased.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the problems and provide a decoloring and hydrolyzing device applied to the preparation of seaweed dietary fibers.
The utility model discloses a following technical scheme realizes above-mentioned purpose:
a decoloration hydrolysis device applied to preparation of seaweed dietary fibers comprises a decoloration hydrolysis tank, a delivery pump and a heat exchange mechanism, wherein one side of the decoloration hydrolysis tank is connected with a temperature control mechanism, the upper end of the decoloration hydrolysis tank is connected with a delivery mechanism, one end of the delivery mechanism is provided with a detection mechanism, the lower end of the decoloration hydrolysis tank is connected with an auxiliary material mechanism, the delivery mechanism, the auxiliary material mechanism and the decoloration hydrolysis tank are all connected through joints, the temperature control mechanism comprises a return water main pipe, a chilled water return pipe, a hot water return pipe and a water inlet main pipe, the chilled water return pipe and the hot water return pipe are connected to the return water main pipe, a spiral temperature adjusting pipe is arranged inside the decoloration hydrolysis tank, one end of the spiral temperature adjusting pipe is connected with the return water main pipe, the other end of the spiral temperature adjusting pipe is connected with the water inlet main pipe, and, detection mechanism is including detecting display, test probe, diaphragm valve, motorised valve, test probe connects on the decoloration jar of hydrolysising, test probe connects the upper end of the test probe detects the display, and level sensor connects decoloration jar of hydrolysising is inboard, conveying mechanism includes material conveying tank, branch material pipe, semi-manufactured goods inlet pipe, finished product discharging pipe, material conveying tank one end is connected the input of delivery pump, delivery pump output end is connected divide the material pipe, divide and connect on the material pipe semi-manufactured goods inlet pipe with the finished product discharging pipe, semi-manufactured goods inlet pipe connects the input of heat transfer mechanism, the material circulating pipe is connected to the output of heat transfer mechanism, connect the material admission pipe on the material circulating pipe, the material admission pipe is connected the decoloration jar of hydrolysising, auxiliary material mechanism includes auxiliary material connecting pipe, the valve is connected to the decoloration, auxiliary material mechanism, The device comprises a steam adding pipe, a decolorant adding pipe and a PH regulator inlet pipe, wherein an auxiliary material connecting pipe is connected to the lower end of a decoloration hydrolysis tank, the decolorant adding pipe and the steam adding pipe are connected to the auxiliary material connecting pipe, the PH regulator inlet pipe is connected to the upper end of the decoloration hydrolysis tank, the steam adding pipe, the decolorant adding pipe, the PH regulator inlet pipe, a material circulating pipe and the material inlet pipe are respectively provided with a diaphragm valve, and a chilled water return pipe, a hot water inlet pipe, a chilled water inlet pipe, a material conveying tank, a semi-finished product inlet pipe, a finished product outlet pipe and the material circulating pipe are respectively provided with an electric valve.
Preferably: the heat exchange mechanism comprises a heat exchange box body, a cooling discharge pipe, a cooling feed pipe and a heat conduction copper pipe, wherein a heat exchange cavity is formed inside the heat exchange box body, the inner side of the heat exchange cavity is connected with the heat conduction copper pipe through a pipe hoop, the input end of the heat conduction copper pipe is connected with the cooling feed pipe, the output end of the heat conduction copper pipe is connected with the cooling discharge pipe, the upper end of the heat exchange box body is connected with a heat exchange water source outlet pipe, one side of the heat exchange water source outlet pipe is provided with a heat exchange water source inlet pipe, and the heat.
So set up, the heat transfer chamber plays through the cooling water effect, heat conduction copper pipe plays the heat transfer effect, the heat transfer box plays sealed effect, has guaranteed joint strength through the ferrule connection.
Preferably: the joint is connected with the decoloration hydrolysis tank through welding.
So set up, connect and play the connection effect, through connect can with the outside through flange joint guaranteed the leakproofness.
Preferably: the detection probe is connected with the decoloring hydrolysis tank through a flange, and the detection display is connected with the detection probe through threads.
So set up, test probe plays detection temperature, pressure, pH value effect, has guaranteed the leakproofness through flange joint.
Preferably: the water return main pipe and the water inlet main pipe are connected with the spiral temperature adjusting pipe through welding.
So set up, the spiral pipe that adjusts the temperature plays the inside temperature control effect, has guaranteed the leakproofness through the welding.
Preferably: the delivery pump is connected with the material delivery tank and the material distributing pipe through flanges.
So set up, the delivery pump plays provides kinetic energy effect, and is inseparable through flange joint.
Preferably: the auxiliary material connecting pipe is connected with the joint through a flange, the material conveying tank is connected with the joint through a flange, the material inlet pipe is connected with the joint through a flange, and the PH regulator inlet pipe is connected with the joint through a flange.
So set up, the joint has guaranteed compactness stability through flange joint.
Preferably: the heat conduction copper pipe is connected with the cooling feeding pipe and the cooling discharging pipe through welding.
So set up, the cooling feed pipe with the cooling discharging pipe plays the connection effect, has guaranteed joint strength through the welding.
Preferably: the heat exchange water source outlet pipe the heat exchange water source inlet pipe is connected with the heat exchange box body through welding.
So set up, heat transfer water source outlet pipe the heat transfer water source inlet tube plays and connects outside heat transfer water source effect.
Preferably: the heat conduction copper pipe is an S-shaped copper pipe.
So set up, utilize S form copper tubulation, can effectively heat conduction and abundant heat transfer.
Compared with the prior art, the beneficial effects of the utility model are as follows:
1. the device has a reasonable structure, adopts external energy and the disc type heat conduction pipe for heating and refrigerating, improves the temperature control efficiency, and simultaneously utilizes the heat exchanger to rapidly cool the material, thereby improving the cooling efficiency;
2. the operation is simple, the electric appliances are connected by using an external controller, the automatic control and processing are realized, and the accuracy and the working efficiency are improved;
3. the safety is high, and the reaction state can be monitored in real time through the detection mechanism, so that the utilization rate of the internal materials and the safety of operators are guaranteed.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings needed to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to these drawings without inventive exercise.
FIG. 1 is a schematic diagram of a first structure of a decoloring and hydrolyzing apparatus for preparing seaweed dietary fiber according to the present invention;
FIG. 2 is a schematic diagram of a second structure of the decolorization hydrolysis device for preparing dietary fiber of seaweed according to the present invention;
FIG. 3 is a schematic structural view of a heat exchange mechanism of the decoloring and hydrolyzing device for preparing seaweed dietary fiber according to the present invention;
FIG. 4 is a schematic diagram of the internal structure of a heat exchange box body of the decoloring and hydrolyzing device for preparing seaweed dietary fiber according to the present invention;
FIG. 5 is a schematic diagram of a spiral temperature-regulating tube structure of a decoloring and hydrolyzing device for preparing seaweed dietary fiber according to the present invention;
FIG. 6 is a schematic view of the internal structure of a decoloring and hydrolyzing tank of a decoloring and hydrolyzing apparatus for preparing seaweed dietary fiber according to the present invention.
The reference numerals are explained below:
1. a decoloring hydrolysis tank; 2. a delivery pump; 3. a heat exchange mechanism; 4. a temperature control mechanism; 5. a detection mechanism; 6. a conveying mechanism; 7. an auxiliary material mechanism; 8. a joint; 31. a heat exchange box body; 32. cooling the discharge pipe; 33. a cooling feed tube; 34. a heat conducting copper pipe; 35. a heat exchange cavity; 36. a heat exchange water source outlet pipe; 37. a heat exchange water source inlet pipe; 41. a water return main pipe; 42. a chilled water return pipe; 43. a hot water return pipe; 44. a water inlet main pipe; 45. a hot water inlet pipe; 46. a chilled water inlet pipe; 47. a spiral temperature regulating tube; 51. detecting a display; 52. detecting a probe; 53. a diaphragm valve; 54. an electrically operated valve; 55. a liquid level sensor; 61. a material conveying tank; 62. distributing pipes; 63. a semi-finished product feeding pipe; 64. a finished product discharge pipe; 65. a material circulating pipe; 66. feeding the material into a pipe; 71. an auxiliary material connecting pipe; 72. a steam addition pipe; 73. a decolorizing agent addition tube; 74. and a pH regulator enters the tube.
Detailed Description
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like, indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are used merely for convenience of description and for simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be construed as limiting the present invention. Furthermore, the terms "first", "second", etc. are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated. Thus, a feature defined as "first," "second," etc. may explicitly or implicitly include one or more of that feature. In the description of the present invention, "a plurality" means two or more unless otherwise specified.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood by those of ordinary skill in the art through specific situations.
The present invention will be further explained with reference to the accompanying drawings:
example 1
As shown in fig. 1-6, a decolorization hydrolysis device for preparing dietary fiber of seaweed comprises a decolorization hydrolysis tank 1, a delivery pump 2 and a heat exchange mechanism 3, wherein one side of the decolorization hydrolysis tank 1 is connected with a temperature control mechanism 4, the upper end of the decolorization hydrolysis tank 1 is connected with a delivery mechanism 6, one end of the delivery mechanism 6 is provided with a detection mechanism 5, the lower end of the decolorization hydrolysis tank 1 is connected with an auxiliary material mechanism 7, the delivery mechanism 6, the auxiliary material mechanism 7 and the decolorization hydrolysis tank 1 are all connected by a joint 8, the temperature control mechanism 4 comprises a return water main 41, a chilled water return pipe 42, a hot water return pipe 43 and a water inlet main 44, the return water main 41 is connected with a chilled water return pipe 42 and a hot water return pipe 43, the inside of the decolorization hydrolysis tank 1 is provided with a spiral temperature adjustment pipe 47, one end of the spiral temperature adjustment pipe 47 is connected with the return water main 41, the other end of the spiral temperature, the detection mechanism 5 comprises a detection display 51, a detection probe 52, a diaphragm valve 53 and an electric valve 54, the detection probe 52 is connected to the decoloration hydrolysis tank 1, the upper end of the detection probe 52 is connected with the detection display 51, the liquid level sensor 55 is connected to the inner side of the decoloration hydrolysis tank 1, the conveying mechanism 6 comprises a material conveying tank 61, a material distribution pipe 62, a semi-finished product feeding pipe 63 and a finished product discharging pipe 64, one end of the material conveying tank 61 is connected with the input end of the conveying pump 2, the output end of the conveying pump 2 is connected with the material distribution pipe 62, the material distribution pipe 62 is connected with the semi-finished product feeding pipe 63 and the finished product discharging pipe 64, the semi-finished product feeding pipe 63 is connected with the input end of the heat exchange mechanism 3, the output end of the heat exchange mechanism 3 is connected with a material circulation pipe 65, the material circulation pipe, Decolourant adds pipe 73, PH regulator admission pipe 74, auxiliary material connecting pipe 71 is connected at 1 lower extreme of decoloration hydrolysis tank, it adds pipe 73 and steam to connect the decolourant on the auxiliary material connecting pipe 71 and adds pipe 72 to add, PH regulator admission pipe 74 is connected in 1 upper end of decoloration hydrolysis tank, steam adds pipe 72, decolourant adds pipe 73, PH regulator admission pipe 74, material circulating pipe 65, all be provided with diaphragm valve 53 on the material admission pipe 66, chilled water wet return 42, hot water wet return 43, hot water inlet tube 45, chilled water inlet tube 46, material conveying jar 61, semi-manufactured goods inlet pipe 63, finished product discharging pipe 64, all be provided with motorised valve 54 on the material circulating pipe 65.
Preferably: the heat exchange mechanism 3 comprises a heat exchange box body 31, a cooling discharge pipe 32, a cooling feed pipe 33 and a heat conduction copper pipe 34, a heat exchange cavity 35 is formed inside the heat exchange box body 31, the inner side of the heat exchange cavity 35 is connected with the heat conduction copper pipe 34 through a pipe hoop, the input end of the heat conduction copper pipe 34 is connected with the cooling feed pipe 33, the output end of the heat conduction copper pipe 34 is connected with the cooling discharge pipe 32, the upper end of the heat exchange box body 31 is connected with a heat exchange water source water outlet pipe 36, one side of the heat exchange water source water outlet pipe 36 is provided with a heat exchange water source water inlet pipe 37, electric valves 54 are arranged on the heat exchange water source water outlet pipe 36 and the heat exchange water source water inlet; the joint 8 is connected with the decoloring hydrolysis tank 1 by welding, the joint 8 plays a role in connection, and the joint 8 can be connected with the outside through a flange, so that the sealing performance is ensured; the detection probe 52 is connected with the decoloring hydrolysis tank 1 through a flange, the detection display 51 is connected with the detection probe 52 through threads, the detection probe 52 plays a role in detecting temperature, pressure and PH value, and the sealing property is ensured through flange connection; the water return header pipe 41 and the water inlet header pipe 44 are connected with the spiral temperature adjusting pipe 47 through welding, the spiral temperature adjusting pipe 47 plays a role in controlling the internal temperature, and the sealing performance is ensured through welding; the conveying pump 2 is connected with the material conveying tank 61 and the material distributing pipe 62 through flanges, and the conveying pump 2 plays a role in providing kinetic energy and is tightly connected through the flanges; the auxiliary material connecting pipe 71 is connected with the joint 8 through a flange, the material conveying tank 61 is connected with the joint 8 through a flange, the material inlet pipe 66 is connected with the joint 8 through a flange, the PH regulator inlet pipe 74 is connected with the joint 8 through a flange, and the joint 8 ensures the tightness stability through flange connection; the heat conduction copper pipe 34 is connected with the cooling feed pipe 33 and the cooling discharge pipe 32 through welding, the cooling feed pipe 33 and the cooling discharge pipe 32 play a role in connection, and the connection strength is ensured through welding; the heat exchange water source outlet pipe 36 and the heat exchange water source inlet pipe 37 are connected with the heat exchange box body 31 through welding, and the heat exchange water source outlet pipe 36 and the heat exchange water source inlet pipe 37 play a role of connecting an external heat exchange water source; the heat conducting copper pipe 34 is an S-shaped copper pipe, and the S-shaped copper pipe can effectively conduct heat and sufficiently exchange heat.
The working principle is as follows: the raw materials are added into the decoloring hydrolysis tank 1 through a material inlet pipe 66, hot water or chilled water is transmitted into a spiral temperature adjusting pipe 47 through controlling an electric valve 54 on a hot water inlet pipe 45 and a chilled water inlet pipe 46 according to the temperature requirement, the temperature of the materials is controlled, then the materials are added into a steam adding pipe 72, a decolorant adding pipe 73 and a PH regulator entering pipe 74, adding auxiliary materials into the decoloring hydrolysis tank 1, starting the delivery pump 2 after the materials react, transmitting the reacted materials into the heat conduction copper pipe 34 through the material distribution pipe 62 and the semi-finished product feeding pipe 63, meanwhile, the electric valves 54 on the heat exchange water source outlet pipe 36 and the heat exchange water source inlet pipe 37 are opened to provide cold water for the interior of the heat exchange cavity 35, so that the materials are cooled and then are transmitted to the interior of the decoloring hydrolysis tank 1 through the material circulating pipe 65, after the reaction is finished, the finished product material is continuously conveyed out through the material conveying tank 61, the material distributing pipe 62 and the finished product discharging pipe 64.
The foregoing illustrates and describes the principles, general features, and advantages of the present invention. It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the foregoing embodiments and descriptions are provided only to illustrate the principles of the present invention without departing from the spirit and scope of the present invention.

Claims (10)

1. A decoloration hydrolysis equipment for preparing seaweed dietary fiber is characterized in that: comprises a decoloration hydrolysis tank (1), a delivery pump (2) and a heat exchange mechanism (3), wherein one side of the decoloration hydrolysis tank (1) is connected with a temperature control mechanism (4), the upper end of the decoloration hydrolysis tank (1) is connected with the delivery mechanism (6), one end of the delivery mechanism (6) is provided with a detection mechanism (5), the lower end of the decoloration hydrolysis tank (1) is connected with an auxiliary material mechanism (7), the delivery mechanism (6), the auxiliary material mechanism (7) and the decoloration hydrolysis tank (1) are connected through a joint (8), the temperature control mechanism (4) comprises a return water main pipe (41), a chilled water return pipe (42), a hot water return pipe (43) and a water inlet main pipe (44), the chilled water return pipe (42) and the hot water return pipe (43) are connected on the return water main pipe (41), a spiral temperature adjusting pipe (47) is arranged inside the decoloration hydrolysis tank (1), spiral temperature adjusting pipe (47) one end is connected return water house steward (41), spiral temperature adjusting pipe (47) other end is connected intake house steward (44), intake house steward (44) are gone up and are connected hot water inlet tube (45) and refrigerated water inlet tube (46), detection mechanism (5) are including detecting display (51), test probe (52), diaphragm valve (53), motorised valve (54), test probe (52) are connected on decoloration hydrolysis tank (1), test probe (52) upper end is connected detect display (51), and level sensor (55) are connected decoloration hydrolysis tank (1) are inboard, conveying mechanism (6) are including material conveying tank (61), branch material pipe (62), semi-manufactured goods inlet pipe (63), finished product discharging pipe (64), material conveying tank (61) one end is connected the input of delivery pump (2), the output end of the conveying pump (2) is connected with the material distributing pipe (62), the material distributing pipe (62) is connected with the semi-finished product inlet pipe (63) and the finished product outlet pipe (64), the semi-finished product inlet pipe (63) is connected with the input end of the heat exchange mechanism (3), the output end of the heat exchange mechanism (3) is connected with the material circulating pipe (65), the material circulating pipe (65) is connected with the material inlet pipe (66), the material inlet pipe (66) is connected with the decoloring hydrolysis tank (1), the auxiliary material mechanism (7) comprises an auxiliary material connecting pipe (71), a steam adding pipe (72), a decoloring agent adding pipe (73) and a PH regulator inlet pipe (74), the auxiliary material connecting pipe (71) is connected with the lower end of the decoloring hydrolysis tank (1), the auxiliary material connecting pipe (71) is connected with the decoloring agent adding pipe (73) and the steam adding pipe (72), PH regulator admission pipe (74) are connected decoloration hydrolysis tank (1) upper end, steam is added pipe (72), decolorant is added pipe (73), PH regulator admission pipe (74) material circulating pipe (65) all be provided with on material admission pipe (66) diaphragm valve (53), refrigerated water wet return (42) hot water wet return (43) hot water inlet tube (45) refrigerated water inlet tube (46) material conveying jar (61) semi-manufactured goods inlet pipe (63) finished product discharging pipe (64) all be provided with on material circulating pipe (65) motorised valve (54).
2. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 1, wherein: heat transfer mechanism (3) are including heat transfer box (31), cooling discharging pipe (32), cooling inlet pipe (33), heat conduction copper pipe (34), heat transfer box (31) inside is provided with heat transfer chamber (35), heat transfer chamber (35) inboard is provided with heat conduction copper pipe (34), heat conduction copper pipe (34) input is connected cooling inlet pipe (33), heat conduction copper pipe (34) output is connected cooling discharging pipe (32), heat transfer water source outlet pipe (36) is connected to heat transfer box (31) upper end, heat transfer water source outlet pipe (36) one side is provided with heat transfer water source inlet tube (37), heat transfer water source outlet pipe (36) with all be provided with on heat transfer water source inlet tube (37) motorised valve (54).
3. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 1, wherein: the joint (8) is connected with the decoloration hydrolysis tank (1) through welding.
4. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 1, wherein: the detection probe (52) is connected with the decoloring hydrolysis tank (1) through a flange, and the detection display (51) is connected with the detection probe (52) through threads.
5. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 1, wherein: the water return main pipe (41) and the water inlet main pipe (44) are connected with the spiral temperature adjusting pipe (47) through welding.
6. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 1, wherein: the delivery pump (2) is connected with the material delivery tank (61) and the material distribution pipe (62) through flanges.
7. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 1, wherein: auxiliary material connecting pipe (71) through flange joint in connect (8), material transport jar (61) passes through flange joint connect (8), material admission pipe (66) pass through flange joint connect (8), PH regulator admission pipe (74) passes through flange joint connect (8).
8. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 2, wherein: the heat conduction copper pipe (34) is connected with the cooling feeding pipe (33) and the cooling discharging pipe (32) through welding.
9. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 2, wherein: the heat exchange water source water outlet pipe (36) and the heat exchange water source water inlet pipe (37) are connected with the heat exchange box body (31) through welding.
10. The decolorization hydrolysis device for preparing dietary fiber of seaweed as claimed in claim 2, wherein: the heat conduction copper pipe (34) is an S-shaped copper pipe.
CN201921977261.3U 2019-11-15 2019-11-15 Be applied to decoloration hydrolysis equipment of preparation marine alga dietary fiber Active CN211430970U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201921977261.3U CN211430970U (en) 2019-11-15 2019-11-15 Be applied to decoloration hydrolysis equipment of preparation marine alga dietary fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201921977261.3U CN211430970U (en) 2019-11-15 2019-11-15 Be applied to decoloration hydrolysis equipment of preparation marine alga dietary fiber

Publications (1)

Publication Number Publication Date
CN211430970U true CN211430970U (en) 2020-09-08

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Application Number Title Priority Date Filing Date
CN201921977261.3U Active CN211430970U (en) 2019-11-15 2019-11-15 Be applied to decoloration hydrolysis equipment of preparation marine alga dietary fiber

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