Medical waste pre-vacuum type sterilization treatment system
Technical Field
The utility model belongs to the technical field of medical waste handles, concretely relates to medical waste is vacuum type sterilization processing system in advance.
Background
The high-temperature steam treatment process for the medical waste is a technical means for killing pathogenic microorganisms by utilizing the heat of water vapor so as to lose infectivity, and in the high-temperature steam treatment of the medical waste, the air of a sterilizer is generally discharged in advance by adopting a vacuumizing mode so as to increase the heat penetrability and improve the heat distribution, thereby ensuring the effect and the efficiency of the medical waste treatment.
The vacuum pump used in the process has two types, one is that a water ring vacuum pump is adopted, and the air in the sterilizer is discharged to the maximum extent by a mode of alternating steam injection and vacuum pumping for many times, wherein the mode is a pulsating vacuum process; another way is to use a steam jet pump to remove air once, which is a pre-vacuum technique.
The general process flow of the pre-vacuum technology is shown in the attached figure 1, the technology adopts 0.8Mpa water vapor as a working medium, on one hand, a water vapor supply pipeline a supplies high-pressure water vapor to a steam jet pump b to enable the steam jet pump to work, then the steam jet pump pumps the interior of a sterilizer c, the vacuum degree of the interior of the sterilizer can be 0.09Mpa, and the gas sprayed by the steam jet pump is condensed by a condenser d; on the other hand, the steam supply line is also communicated with the air inlet of the sterilizer c, and high-temperature steam is used to sterilize the interior of the sterilizer. This pre-vacuum technique suffers from the following disadvantages:
(1) the steam consumption is high;
(2) the noise is extremely high;
(3) a large amount of cooling water is consumed;
(4) part of the odor in the extracted gas exists in the condensed water, so that a certain degree of odor pollution is caused.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome prior art not enough, provide a medical waste vacuum type sterilization processing system in advance.
The utility model discloses a realize through following technical scheme:
a medical waste pre-vacuum type sterilization treatment system comprises a sterilizer, a steam jet pump, a water jet pump, a steam-water separation unit, a cooling unit, a water storage unit and a circulating water pump;
the steam inlet of the sterilizer is connected with a steam supply pipeline, the steam supply pipeline is also communicated with the steam inlet of a steam jet pump, the suction inlet of the steam jet pump is communicated with the gas port at the top of the sterilizer through a pipeline, the outlet of the steam jet pump is communicated with the suction inlet of a water jet pump through a pipeline, the water incident port of the water jet pump is communicated with the water outlet of a circulating water pump through a pipeline, the outlet of the water jet pump is communicated with the inlet of a steam-water separation unit, the water outlet of the steam-water separation unit is connected to the water inlet of a cooling unit through a pipeline, the cooling water outlet of the cooling unit is communicated with the water inlet of a water storage unit, and the water outlet of the water storage unit is communicated with the water inlet of the circulating water pump.
In the technical scheme, the gas outlet of the steam-water separation unit is connected to the deodorization unit through a pipeline, and the gas separated by the steam-water separation unit is processed through the deodorization unit.
The utility model discloses an advantage and beneficial effect do:
1. a water injection pump is connected in series after the steam injection pump to form a two-stage vacuum system, so that the consumption of steam is reduced, and the noise is also reduced.
2. The water jet pump is simultaneously used as a hybrid condenser to perform direct contact heat exchange condensation on the exhaust steam flowing out of the steam jet pump, so that heat exchange of cold and hot fluids can be quickly realized, the vacuumizing effect is increased, and higher vacuum degree is achieved.
3. A steam-water separator is additionally arranged behind the water injection pump, the extracted non-condensable gas and malodorous gas are separated from water, and the non-condensable gas and the malodorous gas enter a specially-arranged deodorization unit under the drainage of a fan, so that the environment pollution is effectively avoided.
4. The working medium for the water injection pump is circulating water, the heated circulating water is cooled by the cooling tower, collected and continuously supplied to the water injection pump by the circulating water pump, so that continuous operation of equipment can be ensured, and water sources are effectively saved.
Drawings
FIG. 1 is a schematic diagram of a prior art pre-vacuum type sterilization system;
fig. 2 is a schematic structural view of the medical waste pre-vacuum type sterilization system of the present invention.
Wherein:
0: steam supply line, 1: sterilizer, 2: steam jet pump, 3: water jet pump, 4: steam-water separation unit, 5: cooling unit, 6: water storage unit, 7: circulating water pump, 8: a deodorization unit.
For a person skilled in the art, other relevant figures can be obtained from the above figures without inventive effort.
Detailed Description
In order to make the technical field person understand the solution of the present invention better, the technical solution of the present invention is further described below with reference to the specific embodiments.
Example one
Referring to fig. 2, the medical waste pre-vacuum type sterilization treatment system comprises a sterilizer 1, a steam injection pump 2, a water injection pump 3, a steam-water separation unit 4, a cooling unit 5, a water storage unit 6 and a circulating water pump 7.
The steam inlet of the sterilizer 1 is connected with a steam supply pipeline 0, the steam supply pipeline is also communicated with the steam inlet of the steam jet pump 2, the suction inlet of the steam jet pump 2 is communicated with the gas port at the top of the sterilizer 1 through a pipeline, the outlet of the steam jet pump 2 is communicated with the suction inlet of the water jet pump 3 through a pipeline, the water incident port of the water jet pump 3 is communicated with the water outlet of the circulating water pump 7 through a pipeline, the outlet of the water jet pump 3 is communicated with the inlet of the steam-water separation unit 4, the water outlet at the bottom of the steam-water separation unit 4 is connected to the water inlet of the cooling unit 5 through a pipeline, the cooling water outlet of the cooling unit 5 is communicated with the water inlet of the water storage unit 6, and the water outlet of the water storage unit 6 is communicated with the water inlet of the circulating water pump 7.
When the sterilizer works, the circulating water pump 7 is started to enable the water injection pump 3 to work, meanwhile, the steam supply pipeline supplies high-pressure steam to the steam injection pump 2 to enable the steam injection pump 2 to work, the water injection pump 3 can generate suction force on the steam injection pump 2 when working, a two-stage vacuum system is formed, the consumption of steam can be reduced, noise is reduced, the vacuumizing effect on the sterilizer 1 can be enhanced, and the interior of the sterilizer can reach higher vacuum degree; the gas-liquid mixture sprayed out of the water jet pump 3 enters a steam-water separation unit 4, water and steam are separated through the steam-water separation unit, the separated liquid enters a cooling unit 5 for cooling, and the cooled liquid enters a water storage unit 6 from the cooling unit so as to supply water for a circulating water pump 7.
Example two
Since the gas withdrawn from the sterilizer contains non-condensable gases and malodorous gases, these gases may cause pollution if discharged directly into the environment. Therefore, in this embodiment, on the basis of the first embodiment, the gas outlet of the steam-water separation unit is connected to the deodorization unit 8 through a pipeline, the top outlet of the deodorization unit 8 is provided with the induced draft fan 8.1, and the gas separated by the steam-water separation unit is treated through the deodorization unit 8.
Spatially relative terms, such as "upper," "lower," "left," "right," and the like, may be used in the embodiments for ease of description to describe one element or feature's relationship to another element or feature as illustrated in the figures. It will be understood that the spatial terms are intended to encompass different orientations of the device in use or operation in addition to the orientation depicted in the figures. For example, if the device in the figures is turned over, elements described as "below" other elements or features would then be oriented "above" the other elements or features. Thus, the exemplary term "lower" can encompass both an upper and a lower orientation. The device may be otherwise oriented (rotated 90 degrees or at other orientations) and the spatially relative descriptors used herein interpreted accordingly.
Moreover, relational terms such as "first" and "second," and the like, may be used solely to distinguish one element from another element having the same name, without necessarily requiring or implying any actual such relationship or order between such elements.
The invention has been described above by way of example, and it should be noted that any simple variants, modifications or other equivalent substitutions by a person skilled in the art without spending creative effort may fall within the scope of protection of the present invention without departing from the core of the present invention.