90results about How to "Simple operation and control" patented technology

The invention provides a reaction cup loading system for automatically conveying reaction cups to an analysis device. The reaction cup loading system comprises a rack, as well as a cup storage cabin, a cup fetching mechanism and a cup conveying mechanism which are fixedly arranged on the rack and are arranged in sequence along a conveying direction of the reaction cups, wherein a cup outlet is formed in the bottom of the cup storage cabin; the cup fetching mechanism comprises a guide pipe, a driver for driving the guide pope to hoist to enable the guide pipe to stretch into the cup storage cabin from the cup outlet to take the cups, and a first mechanical switch for controlling the reaction cups in the guide pipe to fall off one by one from a first outlet; the cup conveying mechanism comprises a slide groove and a second mechanical switch for controlling the reaction cups in the slide groove to slide out one by one from a second outlet; the reaction cup loading system further comprises a cup detection mechanism arranged on the cup fetching mechanism and/or the cup conveying mechanism. A reaction cup automatic conveying device provides guarantees to full-automatic operation of a biological sample analysis system, has a compact whole structure, is simple to operate and control, has low operation fault rate and is accurate and reliable to convey; the device can be continuously operated for a long time with the matching of the detection mechanism, so that the conveying efficiency is improved and the operation cost is reduced.

The invention discloses a device for strengthening anaerobic ammonia oxidation and nitrogen removal process. The device comprises a raw-water storage tank, a feed pump, a biochemical reactor and a continuous flow reactor of a sediment tank; the continuous flow reactor is connected with a PLC (programmable logic controller); the biochemical reactor contains an anaerobic zone, an aerobic zone and an anoxic zone; the urban raw-material storage tank is communicated with a water inlet pipe of the biochemical reactor through the feed pump, and sewage is sequentially connected with the anaerobic zone, the aerobic zone, the anoxic zone and the sediment tank through the water inlet pipe; the sediment tank is subjected to sludge and water separation, and a supernatant is discharged as yielding water; in the anaerobic zone, activated sludge absorbs an organic matter synthesized internal carbon source degraded into the water; in the aerobic zone, coupling of short-cut nitrogen removal and anaerobic ammonium oxidation is realized by controlling dissolved oxygen, and nitrogen removal rate of the system is increased.

The invention provides a molten salt electrode boiler heat storage and power generation system, and belongs to the field of energy storage. The system involves a heating part, a high-temperature molten salt storage tank and a heat utilization part; the heating part comprises a boiler body, a high-voltage electrode, a neutral electrode and a low-temperature molten salt supply head, wherein the high-voltage electrode, the neutral electrode and the low-temperature molten salt supply head are arranged in the boiler body, the high-voltage electrode is used for being connected with a power generation system, and the low-temperature molten salt supply head is used for filling the boiler body with low-temperature molten salt; one end of the high-temperature molten salt storage tank is connected with the bottom of the boiler body, and the other end of the high-temperature molten salt storage tank is connected with the heat utilization part; and the heat utilization part is used for carrying outheat exchange on the molten salt sent out by the high-temperature molten salt storage tank and a water working medium for pushing the steam turbine to act, and sending the cooled molten salt back tothe boiler body. Wind power photovoltaic curtailed electricity is used for heating the molten salt and storing heat in the off-peak period of electricity utilization, and high-temperature molten saltis used for heating feed water to generate high-temperature and high-pressure steam in the peak period of electricity utilization, so that the steam turbine is pushed to act, he stored heat is converted into electric energy to be output, and the curtailed wind and light can be effectively consumed to realize large-scale storage and scheduling of non-water renewable energy power.

The invention belongs to the technical field of water treatment and relates to a purifying treatment method for industrial sewage, in particular to a method and a device for ultraviolet-Fenton reagent-biological joint treatment. The industrial sewage is subject to flocculent settling pre-treatment and then flows into a photocatalytic oxidation pool for photocatalytic reaction so as to further reduce the COD of the sewage and improve the biodegradability thereof. Compared with the prior art, the purifying treatment method overcomes the shortcomings that the conventional biofiltration technology has low treatment efficiency, large occupation area and the like when treating the difficult degradable organic waste water. Meanwhile, the joint process further effectively reduces the defects of incomplete decomposition and production of toxic product caused by the ultraviolet oxidation technology, reduces the potential risk to the environment and the human health and further improves the economical efficiency of sewage treatment.

The invention discloses an organic working medium absorption type power generation method and system driven by a low-temperature heat source. The organic working medium absorption type power generation method driven by the low-temperature heat source comprises the following steps that (1) organic working media are heated into a saturated solution, the saturated solution is led into a first vortex tube, and a gas-liquid two-phase mixture is generated after the first vortex tube expands for depressurization; (2) first superheated steam flowing out of the first vortex tube and first saturated steam are mixed and enter a first expansion machine to expand for acting; and (3) a second solution flowing out of a second vortex tube flows through a regenerative evaporator to release heat under the gravity effect and then enters an absorber, and the first expansion machine and a second expansion machine act to drive a power generator connected with the first expansion machine and the second expansion machine to operate to generate power through couplings. According to the organic working medium absorption type power generation method and system driven by the low-temperature heat source, two-stage separation is conducted on the high-pressure saturated concentrated solution, and generated refrigerant steam is used for expansion acting for power generation; and meanwhile, the pressure in the absorption process of the system is regulated through a circulating pump, and the heat load of a condenser is reduced, so that the heat efficiency of the power generation system is improved, and high technical economical efficiency is achieved.

The invention discloses a device and a method for advanced treatment of sludge anaerobic digestion liquid and municipal sewage by a shortcut nitrification combined multi-stage influent denitrificationammonia oxidation process, belonging to the field of sewage biological treatment. The device adopts a sequencing batch reactor (SBR) and an upflow anaerobic sludge bed (UASB) reactor to operate jointly. The sequencing batch SBR is used to carry out short-cut nitrification of the sludge anaerobic digestion liquid. Effluent enters the UASB reactor from the bottom. The reactor is divided into an anaerobic ammonia oxidation zone, an intermediate mixing zone and a short-cut denitrification coupled anaerobic ammonia oxidation zone from bottom to top. The municipal sewage enters the UASB reactor from a middle water inlet, and the short-range denitrification reaction uses an organic carbon source in the municipal sewage to reduce nitrate generated in the anaerobic ammonia oxidation process to nitrite, and the nitrite and ammonia nitrogen in the municipal sewage are removed through the anaerobic ammonia oxidation, thus realizing synchronous and efficient treatment of the sludge anaerobic digestion liquid and the municipal sewage. The method has the advantages of high denitrification efficiency, saving aeration energy consumption and reducing organic carbon source consumption.

The invention discloses a composite fish-way system for a narrow river valley topography dam, belongs to the technical field of design and construction of ancillary buildings for water conservancy andhydropower engineering, and provides the composite fish-way system which is compact in structure, occupies small space and can open a water supply channel at any time according to the change of the upstream water level. The composite fish-way system comprises cutting devices, migration transition channels, a high concrete dam with multiple fish-way outlets formed in an upstream-side dam body as well as multiple water culverts in the number equivalent to that of the fish-way outlets; the fish-way outlets are formed in the high concrete dam at intervals in the vertical direction; the parts, after passing through the high concrete dam, of the water culverts are connected with the various fish-way outlets correspondingly; downstream-side end openings of the water culverts communicate with corresponding parts of the migration transition channels with the axial central lines perpendicular to the water flow direction; the water culverts located in the positions more than 1.5 m deep below theupstream-side water surface are blocked by the cutting devices; and the composite fish-way structure communicates with the downstream-side water body through the migration transition channels.

The invention provides an indoor sunshading and cooling device with internal cooling water pipes and belongs to the field of building energy-saving technology. The device comprises sunshading louvers and further comprises the cooling water pipes, a cold source, a water pump, a cooling water inlet and a cooling water outlet. The cooling water pipes are distributed on the indoor side of a glass envelop structure in parallel, the sunshading louvers are arranged on the cooling water pipes, and the cooling water pipes are connected with the cold source through the cooling water inlet and the cooling water outlet. The water pump is arranged between a pipeline between the cold source and the cooling water outlet or a pipeline between the cold source and the cooling water inlet. The glass envelop structure is a window or a curtain wall or a ceiling. The light transmittance can be flexibly adjusted through a sunshading louver adjusting mechanism. The cooling water pipes are distributed horizontally or vertically, and the cooling water pipes are connected in series or in parallel. The indoor sunshading and cooling device can keep out solar radiation, heat nearby the indoor sunshading device can be directly removed through high-temperature cooling water, and therefore loads of an air conditioner are substantially reduced in summer, and the indoor sunshading and cooling device is simple in structure and easy to popularize.

The invention discloses a synchronous carbon and nitrogen removing reactor which is suitable for the treatment of waste water with high ammonia nitrogen and low carbon and nitrogen ratio, in particular for the treatment of kitchen waste water, an anaerobic digestion solution and the like which are similar to the waste water with high ammonia nitrogen and low carbon and nitrogen ratio. The synchronous carbon and nitrogen removing reactor mainly comprises a cylindrical inner cylinder body and a cylindrical outer cylinder body which are coaxial, wherein an aeration device, a jet device, filler, an effluent weir and the like are arranged in the cylinder bodies; biological filter as a carrier is distributed in the inner cylinder; flow-separated ball filler as a carrier is put into the outer cylinder; after the anaerobic digestion solution with the high ammonia nitrogen is treated by the reactor, the removal rate of the ammonia and the nitrogen can reach 75 to 90 percent, and the removal rate of CODCr (Chemical Oxygen Demand) can reach 55 to 65 percent.