CVD-Siemens Reactor Process Hydrogen Recycle System

• US 20110206842A1
• Filed: 02/25/2010
• Published: 08/25/2011
• Est. Priority Date: 02/25/2010
• Status: Abandoned Application

• Current Assignee: Savi Research, Inc.
• Original Assignee: Savi Research, Inc.
• Inventors: Lahoti, Sanjeev, Revankar, Vithal
• Application Number:
  US12/712,314
• Publication Number:
  US 20110206842A1
• Time in Patent Office: Days
• US Class Current: 427/248.1
• CPC Class Codes: C01B 33/035 by decomposition or reduction of gaseous or vaporised silicon compounds in the presence of heated filaments of silicon, carbon or a refractory metal, e.g. tantalum or tungsten, or in the presence of heated silicon rods on which the formed silicon is deposited, a silicon rod being obtained, e.g. Siemens process
• CPC Class Codes: C23C 16/24 Deposition of silicon only
• CPC Class Codes: C23C 16/4402 Reduction of impurities in the source gas
• CPC Class Codes: C23C 16/4412 Details relating to the exhausts, e.g. pumps, filters, scrubbers, particle traps
• CPC Class Codes: Y02P 20/129 Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Abstract

A hydrogen recycle process and system for use with chemical vapor deposition (CVD) Siemens type processes is provided. The process results in substantially complete or complete hydrogen utilization and substantially contamination-free or contamination-free hydrogen.

Claims

1. In a CVD-Siemens system including a reactor vessel containing at least one reaction chamber surrounded by a jacket, wherein a pre-heating fluid is circulated in the jacket;

one or more electrode assemblies extending into the reaction chamber wherein each electrode assembly comprises a gas inlet, one or more heat transfer fluid inlets/outlets;

at least one pair of silicon filaments, the filaments connected to each other at their upper ends with a silicon bridge to form a filament/slim rod assembly, each filament/slim rod assembly enclosed in an isolation jacket;

a source of a silicon-bearing gas connected to the interior of the vessel for supplying the gas into the reaction chamber, wherein the reaction chamber includes one or more distributor locations, to produce a reaction and to deposit polycrystalline silicon on the filaments by chemical vapor deposition thereby producing a rod of polycrystalline silicon;

a heat transfer system connected to the jacketed reaction chamber to supply heat transfer fluid to preheat the filaments/slim rod assemblies; and

a power supply, the improvement comprising a hydrogen recovery and recycle system comprising;

a liquid Nitrogen cooling system;

a silane condenser;

a recycle hydrogen cooler; and

a Hydrogen regeneration cooler, a compressor, and one or more interchangers wherein the discharged gas from the reactor is cooled to between about 30 and 40°

C., the compressor accepts and compresses the cooled gas to the system requirement pressure, the interchangers cool an off-gas to between −

160 and −

165°

C. using counter flow between cooler and warmer streams, the off-gas stream is further cooled to between −

170 and −

180°

C. using a liquid nitrogen exchanger in the hydrogen regeneration cooler.

2. The improvement of claim 1 further comprising a knockout drum to accept the gas from the recycle hydrogen cooler wherein a first purified hydrogen gas is separated from silane and impurities and collected from the top of the knockout drum.

3. The improvement of claim 2 further comprising one or more adsorption beds arranged after the knockout drum wherein the hydrogen stream flows through the adsorption beds such that the adsorption beds remove impurity gasses from the hydrogen stream to produce a purified hydrogen stream.

4. The improvement of claim 3 wherein there are two or more adsorption beds arranged in series and producing the purified hydrogen stream.

5. The improvement of claim 3 further comprising a cryogenic filter through which the second purified hydrogen stream is passed to remove fine particles to produce a final purified hydrogen stream.

6. The improvement of claim 5 further comprising means to recycle the final purified hydrogen stream to the reactor.

7. The improvement of claim 1 further comprising a hydrogen storage system.

8. The improvement of claim 1 further comprising a make-up hydrogen supply system.

9. A method for recovery, purification and recycle of hydrogen in a CVD Siemens process comprising:

collecting off gases from a CVD Siemens process reactor;

cooling the off gases;

filtering the off gases;

compressing the off gases to at least about 25 psig;

cooling the compressed off gases to a temperature between about −

160 C and −

165 C and then cooling the compressed off gases againt to a temperature between about −

170 C and −

180 C thereby separating condensed impurities from a hydrogen component of the off gases;

passing the hydrogen component through absorption beds to remove any argon, hydrocarbons, uncondensed silanes, boron and phosphorous compounds from the hydrogen component to obtain a first filtered hydrogen stream;

cryogenically filtering the first filtered hydrogen stream to produce a second filtered hydrogen stream;

heating the second filtered hydrogen stream to between about 25 C and 30 C to produce a high purity hydrogen stream;

passing the high purity hydrogen stream through a recycle hydrogen filter to remove particles having a size between 0.1 and 0.4 microns to produce a final hydrogen recycle stream; and

recycling the final hydrogen recycle stream to the CVD Siemens process reactor.