CN216367928U - Energy-saving Maillard reaction system - Google Patents
Energy-saving Maillard reaction system Download PDFInfo
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- CN216367928U CN216367928U CN202220618986.9U CN202220618986U CN216367928U CN 216367928 U CN216367928 U CN 216367928U CN 202220618986 U CN202220618986 U CN 202220618986U CN 216367928 U CN216367928 U CN 216367928U
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Abstract
The utility model provides an energy-saving Maillard reaction system, which is formed by connecting more than 3 Maillard reaction devices in series; the Maillard reaction equipment comprises a mixing chamber, wherein a heating cavity is arranged outside the mixing chamber, and a heat-insulating layer is arranged outside the heating cavity; the heating cavity is internally provided with a coil pipe, and the coil pipe is connected with a heating pipeline. The energy-saving Maillard reaction system provided by the utility model utilizes a plurality of Maillard reaction devices connected in series, can meet the requirement of rapid heating of a single device, and simultaneously can utilize tail temperature for preheating and maintaining, thereby reducing the energy loss to the maximum extent.
Description
Technical Field
The utility model belongs to the field of Maillard reaction, and particularly relates to energy-saving Maillard reaction equipment.
Background
The Maillard reaction is a common non-enzymatic browning phenomenon, and is also called non-enzymatic browning reaction when being applied to the production and application of food essence. This reaction was originally discovered by the french chemist maillard in 1912 when glycine was co-heated in admixture with glucose and was therefore referred to as the maillard reaction. The addition of the reaction product can have very obvious influence on the color and the fragrance of food, and is mainly applied to food processing of meat products, dairy products, salted meat products and the like.
At present, the Maillard reaction technologies used in industry are all intermittent Maillard reaction technologies, no continuous processing equipment exists, and the intermittent method has the biggest defects of slow temperature rise, uneven heating, obvious difference of products in each batch, discontinuous process, increased packaging and labor cost, large occupied area and low production efficiency.
SUMMERY OF THE UTILITY MODEL
In view of the above, the present invention provides an energy-saving maillard reaction system to overcome the defects in the prior art.
In order to achieve the purpose, the technical scheme of the utility model is realized as follows:
an energy-saving Maillard reaction system is formed by connecting more than 3 Maillard reaction devices in series;
the Maillard reaction equipment comprises a mixing chamber, wherein a heating cavity is arranged outside the mixing chamber, and a heat-insulating layer is arranged outside the heating cavity; the heating cavity is internally provided with a coil pipe, and the coil pipe is connected with a heating pipeline. The system is suitable for Maillard reaction at the reaction temperature of about 100 ℃ and has the best effect. The heating chamber increases heat dissipation area, and conduction heat that can be abundant, the heating mixes in step, is heated more evenly. The steam is firstly fed into the coil pipe, the temperature is quickly raised, and then the hot water is fed, so that the temperature is stable and the time is controllable.
Further, both ends of the heating pipeline are provided with rotary joints.
Further, maillard reaction equipment is also provided with a transmission fluted disc and a rotating motor, wherein the transmission fluted disc is connected with the heating cavity through a fixing frame, and the rotating motor is connected with the transmission fluted disc.
Furthermore, the Maillard reaction equipment is also provided with a steam inlet, a condensed water outlet and a condensed water circulating outlet, the steam inlet is connected with the inlet end of the heating pipeline, the condensed water outlet and the condensed water circulating outlet are both connected with the outlet end of the heating pipeline, and the condensed water outlet is connected with a condensed water tank. The water in the condensate water tank can be used as the configuration water of the reactant to preheat the materials, so that the energy consumption is further reduced. The pressure of the steam acts on the pipe wall, no pressure is applied to the inner container of the mixing chamber, the thickness of the inner wall material can be reduced, and the heat conducting performance is improved.
Further, the number of the Maillard reaction equipment is 3, and the Maillard reaction equipment comprises a Maillard reaction equipment I, a Maillard reaction equipment II and a Maillard reaction equipment III, wherein a condensed water circulation outlet of the Maillard reaction equipment I is connected with an inlet end of a heating pipeline of the Maillard reaction equipment II, a condensed water circulation outlet of the Maillard reaction equipment II is connected with an inlet end of a heating pipeline of the Maillard reaction equipment III, and a condensed water circulation outlet of the Maillard reaction equipment III is connected with an inlet end of a heating pipeline of the Maillard reaction equipment I. The productivity can be adjusted by increasing or decreasing the equipment according to the reaction time. The main body structures of the Maillard reaction devices are the same, and only the connecting pipelines between the Maillard reaction devices are different.
Furthermore, a circulating valve is arranged at the condensed water circulating outlet, an outlet valve is arranged at the condensed water outlet, and an inlet valve is arranged at the steam inlet.
Compared with the prior art, the utility model has the following advantages:
the energy-saving Maillard reaction system provided by the utility model utilizes a plurality of Maillard reaction devices connected in series, can meet the requirement of rapid heating of a single device, and simultaneously can utilize tail temperature for preheating and maintaining, thereby reducing the energy loss to the maximum extent.
The coils of the energy-saving Maillard reaction equipment have the same direction, and water in the coils can be forcibly discharged in the rotating process of the mixing chamber, so that the smoothness of steam is ensured, and the energy-saving Maillard reaction equipment has the forced water drainage capability.
Drawings
The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate an embodiment of the utility model and, together with the description, serve to explain the utility model and not to limit the utility model. In the drawings:
FIG. 1 is a schematic diagram of an energy efficient Maillard reaction system according to an embodiment of the present invention;
FIG. 2 is a schematic diagram of an energy-saving Maillard reaction apparatus according to an embodiment of the present invention;
fig. 3 is a top view of a heating chamber according to an embodiment of the present invention.
Description of reference numerals:
1. a mixing chamber; 2. a heating cavity; 3. a coil pipe; 4. a heat-insulating layer; 5. a rotary joint; 6. a transmission fluted disc; 7. a fixed mount; 8. a rotating electric machine; 9. heating the pipeline; 10. a condensed water outlet; 11. a condensate water circulation outlet; 12. an outlet valve; 13. a circulation valve; 14. an inlet valve; 15. a condensate tank.
Detailed Description
It should be noted that the embodiments and features of the embodiments may be combined with each other without conflict.
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 those shown in the drawings, and are used only for convenience in describing the present invention and for simplicity in description, and do not indicate or imply that the referenced devices or elements must have a particular orientation, be constructed and operated in a particular orientation, and thus, are not to 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 should be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; 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 described in detail below with reference to the embodiments with reference to the attached drawings.
As shown in fig. 1-3, an energy-saving maillard reaction system is formed by connecting 3 maillard reaction devices in series; the Maillard reaction equipment comprises a mixing chamber 1, wherein a heating cavity 2 is arranged outside the mixing chamber 1, and a heat-insulating layer 4 is arranged outside the heating cavity 2; heating chamber 2 in be provided with coil pipe 3, coil pipe 3 link to each other with heating pipeline 9. The system is suitable for Maillard reaction at the reaction temperature of about 100 ℃ and has the best effect. Heating chamber 2 has increased heat radiating area, and conduction heat that can be abundant, the heating mixes in step, is heated more evenly. The steam is firstly fed into the coil pipe 3, the temperature is quickly raised, and then the hot water is fed, so that the temperature is stable and the time is controllable.
And rotary joints 5 are arranged at two ends of the heating pipeline 9. Maillard reaction unit still be provided with transmission fluted disc 6, rotating electrical machines 8, transmission fluted disc 6 pass through mount 7 with heating chamber 2 link to each other, rotating electrical machines 8 with transmission fluted disc 6 link to each other. The transmission fluted disc 6 and the mixing chamber 1 are erected on the fixed seat and are rotationally connected with the fixed seat, the fixed seat plays a supporting role, and the connection mode and the structure are designed conventionally.
The Maillard reaction equipment is also provided with a steam inlet, a condensed water outlet 10 and a condensed water circulating outlet 11, the steam inlet is connected with the inlet end 9 of the heating pipeline, the condensed water outlet 10 and the condensed water circulating outlet 11 are both connected with the outlet end of the heating pipeline 9, and the condensed water outlet 10 is connected with a condensed water tank 15. The water in the condensed water tank 15 can be used as the configuration water of the reactant to preheat the materials, so that the energy consumption is further reduced. The pressure of the steam acts on the pipe wall, no pressure is applied to the inner container of the mixing chamber 1, the thickness of the inner wall material can be reduced, and the heat conducting performance is improved.
The number of the Maillard reaction equipment is 3, and the Maillard reaction equipment I, the Maillard reaction equipment II and the Maillard reaction equipment III are respectively arranged, a condensate water circulating outlet 11 of the Maillard reaction equipment I is connected with an inlet end of a heating pipeline 9 of the Maillard reaction equipment II, a condensate water circulating outlet 11 of the Maillard reaction equipment II is connected with an inlet end of the heating pipeline 9 of the Maillard reaction equipment III, and a condensate water circulating outlet 11 of the Maillard reaction equipment III is connected with an inlet end of the heating pipeline 9 of the Maillard reaction equipment I. The productivity can be adjusted by increasing or decreasing the equipment according to the reaction time. The condensed water circulating outlet 11 is provided with a circulating valve 13, the condensed water outlet 10 is provided with an outlet valve 12, and the steam inlet is provided with an inlet valve 14.
The implementation process is as follows:
1. preheating: opening an inlet valve 14 of the Maillard reaction equipment I, enabling steam to flow into the coil 3 from the rotary adapter 5, opening a circulating valve 13 of the Maillard reaction equipment I, enabling the Maillard reaction equipment I and the Maillard reaction equipment II to be connected in series, opening the circulating valve 13 of the Maillard reaction equipment II, enabling the Maillard reaction equipment II and the Maillard reaction equipment III to be connected in series, and opening an outlet valve 12 of the Maillard reaction equipment III;
2. feeding and temperature control: feeding materials into a Maillard reaction device I, heating a mixing chamber 1 to a required temperature, starting a rotating motor 8, driving a transmission fluted disc 6 to rotate by the rotating motor 8, and driving the mixing chamber 1 to rotate by the transmission fluted disc 6 through a fixed frame 7, so that the Maillard reaction is smoothly carried out;
3. closing an inlet valve 14 and a circulating valve 13 of the Maillard reaction equipment I, opening an inlet valve 14 of the Maillard reaction equipment II, a circulating valve 13 of the Maillard reaction equipment III and an outlet valve 12 of the Maillard reaction equipment I, and closing an outlet valve 12 of the Maillard reaction equipment III;
4. feeding and temperature control: feeding the materials into a Maillard reaction device II, heating the mixing chamber 1 to a required temperature, starting a rotating motor 8, driving a transmission fluted disc 6 to rotate by the rotating motor 8, and driving the mixing chamber 1 to rotate by the transmission fluted disc 6 through a fixed frame 7, so that the Maillard reaction is smoothly carried out;
5. closing an inlet valve 14 and a circulating valve 13 of the Maillard reaction equipment II, opening an inlet valve 14 of the Maillard reaction equipment III, a circulating valve 13 of the Maillard reaction equipment I and an outlet valve 12 of the Maillard reaction equipment II, and closing an outlet valve 12 of the Maillard reaction equipment I and an outlet valve 12 of the Maillard reaction equipment III;
6. feeding and temperature control: feeding the materials into a Maillard reaction device III, heating the mixing chamber 1 to a required temperature, starting a rotating motor 8, driving a transmission fluted disc 6 to rotate by the rotating motor 8, and driving the mixing chamber 1 to rotate by the transmission fluted disc 6 through a fixed frame 7, so that the Maillard reaction is smoothly carried out;
7. turning off the rotating motor 8, discharging the material from the Maillard reaction equipment I, and then feeding the material for the next reaction;
8. turning off the rotating motor 8, discharging by the Maillard reaction equipment II, and then feeding for the next reaction;
9. and (4) turning off the rotating motor 8, discharging the material from the Maillard reaction equipment III, and then feeding the material for the next reaction.
The above description is only for the purpose of illustrating the preferred embodiments of the present invention and is not to be construed as limiting the utility model, and any modifications, equivalents, improvements and the like that fall within the spirit and principle of the present invention are intended to be included therein.
Claims (6)
1. An energy-saving Maillard reaction system, characterized in that: the system is formed by connecting more than 3 Maillard reaction devices in series;
the Maillard reaction equipment comprises a mixing chamber, wherein a heating cavity is arranged outside the mixing chamber, and a heat-insulating layer is arranged outside the heating cavity; the heating cavity is internally provided with a coil pipe, and the coil pipe is connected with a heating pipeline.
2. The energy efficient maillard reaction system of claim 1, wherein: and rotary joints are arranged at two ends of the heating pipeline.
3. The energy efficient maillard reaction system of claim 1, wherein: maillard reaction unit still be provided with transmission fluted disc, rotating electrical machines, the transmission fluted disc pass through the mount with the heating chamber link to each other, rotating electrical machines with the transmission fluted disc link to each other.
4. The energy efficient maillard reaction system of claim 2, wherein: the Maillard reaction equipment is also provided with a steam inlet, a condensate outlet and a condensate circulation outlet, wherein the steam inlet is connected with the inlet end of the heating pipeline, the condensate outlet and the condensate circulation outlet are both connected with the outlet end of the heating pipeline, and the condensate outlet is connected with a condensate tank.
5. The energy efficient maillard reaction system of claim 4, wherein: the number of the Maillard reaction equipment is 3, and the Maillard reaction equipment I, the Maillard reaction equipment II and the Maillard reaction equipment III are respectively arranged, a condensate water circulating outlet of the Maillard reaction equipment I is connected with an inlet end of a heating pipeline of the Maillard reaction equipment II, a condensate water circulating outlet of the Maillard reaction equipment II is connected with an inlet end of a heating pipeline of the Maillard reaction equipment III, and a condensate water circulating outlet of the Maillard reaction equipment III is connected with an inlet end of a heating pipeline of the Maillard reaction equipment I.
6. The energy efficient maillard reaction system of claim 5, wherein: the condensed water circulating outlet is provided with a circulating valve, the condensed water outlet is provided with an outlet valve, and the steam inlet is provided with an inlet valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220618986.9U CN216367928U (en) | 2022-03-22 | 2022-03-22 | Energy-saving Maillard reaction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202220618986.9U CN216367928U (en) | 2022-03-22 | 2022-03-22 | Energy-saving Maillard reaction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216367928U true CN216367928U (en) | 2022-04-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202220618986.9U Active CN216367928U (en) | 2022-03-22 | 2022-03-22 | Energy-saving Maillard reaction system |
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| CN (1) | CN216367928U (en) |
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- 2022-03-22 CN CN202220618986.9U patent/CN216367928U/en active Active
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