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CN-224212597-U - Integrated feather treatment equipment

CN224212597UCN 224212597 UCN224212597 UCN 224212597UCN-224212597-U

Abstract

The utility model discloses integrated feather processing equipment, which relates to the technical field of feather processing and comprises a primary enzymolysis tank, wherein the output end of the primary enzymolysis tank is communicated with a horizontal centrifuge through a pumping system, the output end of the horizontal centrifuge is communicated with a collecting tank through a pipeline, the output end of the collecting tank is communicated with a first storage tank through a pumping system, the output end of the first storage tank is communicated with a secondary enzymolysis tank through a pumping system, the output end of the secondary enzymolysis tank is communicated with a first flat centrifuge through a pumping system, and the output end of the first flat centrifuge is communicated with a second storage tank through a pumping system.

Inventors

  • LIAN YURONG
  • SU JINHAN

Assignees

  • 广东锐丰肥业有限公司

Dates

Publication Date
20260508
Application Date
20250427

Claims (7)

  1. 1. The integrated feather treatment equipment comprises a primary enzymolysis tank (1), and is characterized in that the output end of the primary enzymolysis tank (1) is communicated with a horizontal centrifuge (2) through a pumping system, the output end of the horizontal centrifuge (2) is communicated with a collecting tank (3) through a pipeline, the output end of the collecting tank (3) is communicated with a first storage tank (4) through a pumping system, the output end of the first storage tank (4) is communicated with a second-stage enzymolysis tank (5) through a pumping system, the output end of the second-stage enzymolysis tank (5) is communicated with a first flat centrifuge (6) through a pumping system, the output end of the first flat centrifuge (6) is communicated with a second storage tank (7) through a pumping system, the output end of the second storage tank (7) is communicated with a second flat centrifuge (9) through a pumping system, the output end of the second flat centrifuge (9) is communicated with a third storage tank (10) through a pumping system, the output end of the second flat centrifuge (7) is communicated with a third flat centrifuge (12) through a concentrating module (12), the output end of the ultra-filtration nano system (13) is communicated with two fourth storage tanks (14) through an electric control three-way pipeline, the output end of each fourth storage tank (14) is communicated with a high-speed dispersion tank (15) through a pumping system, the output end of each high-speed dispersion tank (15) is communicated with a colloid mill (16) through a pipeline, and the output end of each colloid mill (16) is communicated with a low-speed stirring tank (17) through a pumping system.
  2. 2. The integrated feather processing equipment according to claim 1 is characterized in that a temperature control system, a stirring device and an acid-base regulating device are arranged on the primary enzymolysis tank (1), the secondary enzymolysis tank (5) and the low-temperature enzymolysis tank (8).
  3. 3. The integrated feather processing equipment according to claim 2 is characterized in that the temperature control systems on the primary enzymolysis tank (1), the secondary enzymolysis tank (5) and the low-temperature enzymolysis tank (8) comprise jackets and temperature sensors, and the detection ends of the temperature sensors penetrate through and extend to the interiors of the primary enzymolysis tank (1), the secondary enzymolysis tank (5) and the low-temperature enzymolysis tank (8).
  4. 4. The integrated feather processing equipment according to claim 2 is characterized in that the acid-base adjusting devices of the primary enzymolysis tank (1), the secondary enzymolysis tank (5) and the low-temperature enzymolysis tank (8) comprise an acid-base liquid adding pipeline and a PH value sensor, and the detection end of the PH value sensor penetrates through and extends to the inside of the primary enzymolysis tank (1), the secondary enzymolysis tank (5) and the low-temperature enzymolysis tank (8).
  5. 5. The integrated feather processing equipment of claim 1, wherein the horizontal centrifugal machine (2) controls the separation frequency through double motors, and a flat plate filtering structure is arranged at a discharge hole of the horizontal centrifugal machine (2).
  6. 6. The integrated feather processing device of claim 1, wherein the concentration module (11) is a single-effect evaporator combined with a vacuum pump and a steam heating system.
  7. 7. The integrated feather processing device as claimed in claim 1, wherein the discharge port of the low-speed stirring tank (17) is connected with the split charging device.

Description

Integrated feather treatment equipment Technical Field The utility model relates to the technical field of feather treatment, in particular to integrated feather treatment equipment. Background The traditional feather treatment mode mostly adopts compost fermentation, and has the problems of long treatment period, high microorganism screening difficulty, high nitrogen loss, high secondary pollution risk and the like. Therefore, the problems of low enzymolysis efficiency, low yield and insufficient integration degree of equipment, low process connection efficiency and high energy consumption exist in the prior art, and therefore, the integrated feather processing equipment is provided so as to solve the problems. Disclosure of utility model The utility model aims to provide integrated feather processing equipment so as to solve the problems of low enzymolysis efficiency, low yield and insufficient integration degree of equipment, low process connection efficiency and high energy consumption in the prior art. In order to achieve the aim, the integrated feather processing equipment comprises a primary enzymolysis tank, wherein the output end of the primary enzymolysis tank is communicated with a horizontal centrifuge through a pumping system, the output end of the horizontal centrifuge is communicated with a collecting tank through a pipeline, the output end of the collecting tank is communicated with a first storage tank through the pumping system, the output end of the first storage tank is communicated with a secondary enzymolysis tank through the pumping system, the output end of the secondary enzymolysis tank is communicated with a first flat-plate centrifuge through the pumping system, the output end of the first flat-plate centrifuge is communicated with a second storage tank through the pumping system, the output end of the second storage tank is communicated with a low-temperature enzymolysis tank through the pumping system, the output end of the low-temperature enzymolysis tank is communicated with a second flat-plate centrifuge through the pumping system, the output end of the second flat-plate centrifuge is communicated with a third storage tank through the pumping system, the output end of the third flat-plate centrifuge is communicated with a concentration module through the pipeline, the output end of the concentration module is communicated with a third flat-plate centrifuge through the pumping system, the output end of the third flat-plate centrifuge is communicated with the second flat-plate centrifuge through the high-speed dispersing tank through the pumping system, and the high-speed dispersing tank is communicated with the output end of the high-speed dispersing tank through the high-speed dispersing tank, and the high-speed dispersing tank is communicated with the high-speed dispersing tank through the high-speed dispersing tank. Preferably, the temperature control system, the stirring device and the acid-base regulating device are arranged on the primary enzymolysis tank, the secondary enzymolysis tank and the low-temperature enzymolysis tank. Preferably, the temperature control systems on the primary enzymolysis tank, the secondary enzymolysis tank and the low-temperature enzymolysis tank comprise jackets and temperature sensors, and the detection ends of the temperature sensors penetrate through and extend to the interiors of the primary enzymolysis tank, the secondary enzymolysis tank and the low-temperature enzymolysis tank. Preferably, the acid-base adjusting device of the primary enzymolysis tank, the secondary enzymolysis tank and the low-temperature enzymolysis tank comprises an acid-base liquid adding pipeline and a PH value sensor, and the detection end of the PH value sensor penetrates through and extends to the inside of the primary enzymolysis tank, the secondary enzymolysis tank and the low-temperature enzymolysis tank. Preferably, the horizontal centrifugal machine controls the separation frequency through double motors, and a flat plate filtering structure is arranged at the discharge hole of the horizontal centrifugal machine. Preferably, the concentration module is a single-effect evaporator combined with a vacuum pump and a steam heating system. Preferably, the discharge port of the low-speed stirring tank is connected with the split charging equipment. Compared with the prior art, the utility model has the beneficial effects that: (1) According to the utility model, each module is in seamless connection through the pipeline and the pumping system, so that intermediate transfer links are reduced, integrated processing treatment is realized, and the treatment efficiency is improved. (2) Through tertiary enzymolysis tank, every enzymolysis tank all disposes independent temperature control device, but regional control pH valve and the input of different complex enzymes ensure the best condition of different stage enzymolysis reaction. (3) And temperature and PH value sen